TWI608117B - Film forming method - Google Patents

Film forming method Download PDF

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TWI608117B
TWI608117B TW104142883A TW104142883A TWI608117B TW I608117 B TWI608117 B TW I608117B TW 104142883 A TW104142883 A TW 104142883A TW 104142883 A TW104142883 A TW 104142883A TW I608117 B TWI608117 B TW I608117B
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gas
substrate
film
film forming
plasma
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TW201639981A (en
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小山峻史
吹上紀明
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東京威力科創股份有限公司
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    • HELECTRICITY
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    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
    • H01L21/02Manufacture or treatment of semiconductor devices or of parts thereof
    • H01L21/02104Forming layers
    • H01L21/02107Forming insulating materials on a substrate
    • H01L21/02109Forming insulating materials on a substrate characterised by the type of layer, e.g. type of material, porous/non-porous, pre-cursors, mixtures or laminates
    • H01L21/02112Forming insulating materials on a substrate characterised by the type of layer, e.g. type of material, porous/non-porous, pre-cursors, mixtures or laminates characterised by the material of the layer
    • H01L21/02123Forming insulating materials on a substrate characterised by the type of layer, e.g. type of material, porous/non-porous, pre-cursors, mixtures or laminates characterised by the material of the layer the material containing silicon
    • H01L21/0217Forming insulating materials on a substrate characterised by the type of layer, e.g. type of material, porous/non-porous, pre-cursors, mixtures or laminates characterised by the material of the layer the material containing silicon the material being a silicon nitride not containing oxygen, e.g. SixNy or SixByNz
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    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/22Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the deposition of inorganic material, other than metallic material
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    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/455Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
    • C23C16/45523Pulsed gas flow or change of composition over time
    • C23C16/45525Atomic layer deposition [ALD]
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    • C23C16/45536Use of plasma, radiation or electromagnetic fields
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    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C16/00Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes
    • C23C16/44Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating
    • C23C16/455Chemical coating by decomposition of gaseous compounds, without leaving reaction products of surface material in the coating, i.e. chemical vapour deposition [CVD] processes characterised by the method of coating characterised by the method used for introducing gases into reaction chamber or for modifying gas flows in reaction chamber
    • C23C16/45523Pulsed gas flow or change of composition over time
    • C23C16/45525Atomic layer deposition [ALD]
    • C23C16/45544Atomic layer deposition [ALD] characterized by the apparatus
    • C23C16/45548Atomic layer deposition [ALD] characterized by the apparatus having arrangements for gas injection at different locations of the reactor for each ALD half-reaction
    • C23C16/45551Atomic layer deposition [ALD] characterized by the apparatus having arrangements for gas injection at different locations of the reactor for each ALD half-reaction for relative movement of the substrate and the gas injectors or half-reaction reactor compartments
    • HELECTRICITY
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    • H01L21/00Processes or apparatus adapted for the manufacture or treatment of semiconductor or solid state devices or of parts thereof
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    • H01L21/022Forming insulating materials on a substrate characterised by the type of layer, e.g. type of material, porous/non-porous, pre-cursors, mixtures or laminates the layer being a laminate, i.e. composed of sublayers, e.g. stacks of alternating high-k metal oxides
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    • H01L21/0226Forming insulating materials on a substrate characterised by the process for the formation of the insulating layer formation by a deposition process
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    • H01L21/02107Forming insulating materials on a substrate
    • H01L21/02225Forming insulating materials on a substrate characterised by the process for the formation of the insulating layer
    • H01L21/0226Forming insulating materials on a substrate characterised by the process for the formation of the insulating layer formation by a deposition process
    • H01L21/02263Forming insulating materials on a substrate characterised by the process for the formation of the insulating layer formation by a deposition process deposition from the gas or vapour phase
    • H01L21/02271Forming insulating materials on a substrate characterised by the process for the formation of the insulating layer formation by a deposition process deposition from the gas or vapour phase deposition by decomposition or reaction of gaseous or vapour phase compounds, i.e. chemical vapour deposition
    • H01L21/0228Forming insulating materials on a substrate characterised by the process for the formation of the insulating layer formation by a deposition process deposition from the gas or vapour phase deposition by decomposition or reaction of gaseous or vapour phase compounds, i.e. chemical vapour deposition deposition by cyclic CVD, e.g. ALD, ALE, pulsed CVD

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Description

成膜方法Film formation method

本申請案主張以2014年12月24日申請之日本申請案特願2014-259976號為基礎的優先權,且在此加入其全部揭示內容。Priority is claimed on the basis of Japanese Patent Application No. 2014-259976, filed on Dec.

本發明之各種方面及實施形態係關於成膜方法。Various aspects and embodiments of the present invention relate to a film forming method.

矽基板會因暴露於大氣中,而在表面上形成薄自然氧化膜。若在矽基板上形成自然氧化膜,在矽基板上形成SiN膜時,產生SiN膜之異常成長。為防止這種情形,在將矽基板搬送至反應爐後,在矽基板上形成由基板表面相關性小之SiON系薄膜構成的基底膜,並連續形成SiN系薄膜的技術是習知的。 請參照日本特開平7-245268號公報The ruthenium substrate forms a thin natural oxide film on the surface due to exposure to the atmosphere. When a natural oxide film is formed on the germanium substrate and an SiN film is formed on the germanium substrate, abnormal growth of the SiN film occurs. In order to prevent such a situation, it is known to form a base film made of a SiON-based film having a small surface correlation on a substrate, and to continuously form a SiN-based film, after the substrate is transferred to a reaction furnace. Please refer to Japanese Patent Laid-Open No. 7-245268

在一實施形態中,揭示之成膜方法係在載置於成膜裝置之處理容器內並具有含有碳原子之含碳膜的被處理基板上,形成氮化膜,且該成膜方法包含第1氮化膜形成步驟,而該第1氮化膜形成步驟係藉由包含不具有氫原子之氮化物氣體及惰性氣體的第1反應氣體的電漿,在含碳膜上形成第1氮化膜。In one embodiment, the film forming method is disclosed in which a nitride film is formed on a substrate to be processed which is placed in a processing container of a film forming apparatus and has a carbon-containing film containing carbon atoms, and the film forming method includes 1 a nitride film forming step of forming a first nitridation on a carbon-containing film by a plasma containing a first reaction gas of a nitride gas having no hydrogen atoms and an inert gas; membrane.

上述概要只是用以說明,沒有要以任何方式限制之意圖。除了上述說明之態樣、實施例及特徵外,追加之態樣、實施例及特徵亦可藉由參照圖式及以下詳細之說明而變得明確。The above summary is for illustrative purposes only and is not intended to be limiting in any way. In addition to the above-described aspects, embodiments, and features, additional aspects, embodiments, and features may be

在以下詳細說明中,參照形成說明書之一部分的添附圖式。詳細說明、圖式及申請專利範圍記載之說明實施例不是意圖限制。在不偏離在此所示之本發明的思想或範圍之情形下,可使用其他實施例,且可進行其他變形。In the following detailed description, reference is made to the accompanying drawings which form a part of the specification. The detailed description, the drawings and the description of the claims are not intended to be limiting. Other embodiments may be utilized, and other variations may be made, without departing from the spirit and scope of the inventions.

以含有碳原子之膜作為基底膜,並在該基底膜上形成氮化膜時,有時電漿中之離子與基底膜包含之碳原子反應,使基底膜分解。因此,難以維持含有碳原子之基底膜的厚度,並在基底膜上形成預定厚度之氮化膜。特別在藉由原子層沉積(ALD;Atomic Layer Deposition)法在基板上形成氮化膜時,由於成膜速度慢且基底膜與電漿接觸之時間長,使吸附在基底膜表面上之分子氮化時,在分子與基底膜之間產生不需要之反應。因此,產生基底膜之分解或氮化膜之劣化。When a film containing a carbon atom is used as a base film and a nitride film is formed on the base film, ions in the plasma may react with carbon atoms contained in the base film to decompose the base film. Therefore, it is difficult to maintain the thickness of the base film containing carbon atoms, and a nitride film of a predetermined thickness is formed on the base film. In particular, when a nitride film is formed on a substrate by an Atomic Layer Deposition (ALD) method, molecular nitrogen adsorbed on the surface of the base film is caused by a slow film formation speed and a long time for the base film to contact the plasma. When it is formed, an unwanted reaction occurs between the molecule and the base film. Therefore, decomposition of the base film or deterioration of the nitride film occurs.

在一實施形態中,揭示之成膜方法係在載置於成膜裝置之處理容器內並具有含有碳原子之含碳膜的被處理基板上,形成氮化膜,且該成膜方法包含第1氮化膜形成步驟,而該第1氮化膜形成步驟係藉由包含不具有氫原子之氮化物氣體及惰性氣體的第1反應氣體的電漿,在含碳膜上形成第1氮化膜。In one embodiment, the film forming method is disclosed in which a nitride film is formed on a substrate to be processed which is placed in a processing container of a film forming apparatus and has a carbon-containing film containing carbon atoms, and the film forming method includes 1 a nitride film forming step of forming a first nitridation on a carbon-containing film by a plasma containing a first reaction gas of a nitride gas having no hydrogen atoms and an inert gas; membrane.

此外,在揭示之成膜方法的一實施形態中,在第1氮化膜形成步驟中,第1氮化膜宜藉由ALD法形成。Further, in an embodiment of the film forming method disclosed, in the first nitride film forming step, the first nitride film is preferably formed by an ALD method.

另外,在揭示之成膜方法的一實施形態中,第1反應氣體宜為N2 氣體與Ar氣體之混合氣體。Further, in an embodiment of the film forming method disclosed, the first reaction gas is preferably a mixed gas of N 2 gas and Ar gas.

再者,在揭示之成膜方法的一實施形態中,N2 氣體流量對Ar氣體流量之比率宜為1/50以下。Further, in an embodiment of the film forming method disclosed, the ratio of the flow rate of the N 2 gas to the flow rate of the Ar gas is preferably 1/50 or less.

此外,在揭示之成膜方法的一實施形態中,第1氮化膜形成步驟宜藉由從天線供給至處理容器內之微波產生第1反應氣體的電漿,且由天線供給至處理容器內之微波的功率總和為2kW以上。Further, in an embodiment of the film forming method disclosed, the first nitride film forming step preferably generates a plasma of the first reaction gas by microwaves supplied from the antenna into the processing container, and is supplied from the antenna to the processing container. The sum of the power of the microwaves is 2 kW or more.

另外,揭示之成膜方法,在一實施形態中,宜包含第2氮化膜形成步驟,而該第2氮化膜形成步驟係在第1氮化膜形成步驟後,藉由包含與第1反應氣體不同之氣體的第2反應氣體的電漿,在第1氮化膜上,形成第2氮化膜。Further, in the film forming method disclosed, in one embodiment, it is preferable to include a second nitride film forming step, and the second nitride film forming step is included in the first nitride film forming step, and is included in the first A plasma of the second reaction gas of a gas having a different reaction gas forms a second nitride film on the first nitride film.

再者,在揭示之成膜方法的一實施形態中,第2反應氣體中宜包含含有氫原子之氮化物氣體。Further, in an embodiment of the film forming method disclosed, it is preferable that the second reaction gas contains a nitride gas containing a hydrogen atom.

此外,在揭示之成膜方法的一實施形態中,處理容器宜載置被處理基板,且藉由旋轉設置成可以軸線為中心旋轉之載置台使被處理基板環繞軸線之周圍移動,沿被處理基板相對軸線移動之周方向分成多數區域。另外,第1氮化膜形成步驟宜包含以下步驟:將前驅物氣體供給至多數區域中之一區域,使前驅物氣體之分子吸附在被處理基板之表面;將第1反應氣體供給至多數區域中之另一區域;及藉由供給至多數區域中之另一區域的微波產生第1反應氣體的電漿,並藉由產生之電漿,對吸附有前驅物氣體分子之被處理基板的表面進行電漿處理。再者,第2氮化膜形成步驟宜包含以下步驟:在多數區域中之一區域將前驅物氣體供給至處理容器內,使前驅物氣體之分子吸附在被處理基板之表面;將第2反應氣體供給至多數區域中之另一區域;及藉由供給至多數區域中之另一區域的微波產生第2反應氣體的電漿,並藉由產生之電漿,對吸附有前驅物氣體分子之被處理基板的表面進行電漿處理。In addition, in an embodiment of the film forming method disclosed, the processing container preferably mounts the substrate to be processed, and the substrate to be processed is moved around the axis by rotating the mounting table that can be rotated about the axis. The circumferential direction in which the substrate moves relative to the axis is divided into a plurality of regions. Further, the first nitride film forming step preferably includes the steps of: supplying a precursor gas to one of a plurality of regions, adsorbing molecules of the precursor gas on the surface of the substrate to be processed; and supplying the first reaction gas to the plurality of regions Another region in the middle; and a plasma of the first reaction gas generated by microwaves supplied to another of the plurality of regions, and the surface of the substrate to be processed to which the precursor gas molecules are adsorbed is generated by the generated plasma Perform plasma treatment. Further, the second nitride film forming step preferably includes the steps of: supplying a precursor gas into the processing container in one of the plurality of regions, adsorbing molecules of the precursor gas on the surface of the substrate to be processed; and performing the second reaction The gas is supplied to another one of the plurality of regions; and the plasma of the second reactive gas is generated by the microwave supplied to the other of the plurality of regions, and the precursor gas molecules are adsorbed by the generated plasma The surface of the substrate to be processed is subjected to plasma treatment.

另外,在揭示之成膜方法的一實施形態中,第1氮化膜宜以0.5nm至1.0nm之厚度形成於含碳膜上。Further, in an embodiment of the film forming method disclosed, the first nitride film is preferably formed on the carbon-containing film with a thickness of 0.5 nm to 1.0 nm.

依據本發明之各種方面及實施形態,可抑制含有碳原子之基底膜的膜厚減少,且在基底膜上形成預定厚度之氮化膜。 (實施形態)According to various aspects and embodiments of the present invention, it is possible to suppress a decrease in film thickness of a base film containing carbon atoms, and to form a nitride film having a predetermined thickness on the base film. (embodiment)

圖1係顯示成膜裝置10之一例的剖面圖。圖2係顯示由上方看時之成膜裝置10之一例的示意圖。圖2中之A-A剖面係圖1。圖3及圖4係顯示圖1中軸線X左側部分之一例的放大剖面圖。圖5係顯示單元U下面之一例的圖。圖6係顯示圖1中軸線X右側部分之一例的放大剖面圖。圖1至圖6所示之成膜裝置10主要具有處理容器12、載置台14、第1氣體供給部16、排氣部18、第2氣體供給部20及電漿產生部22。FIG. 1 is a cross-sectional view showing an example of the film forming apparatus 10. Fig. 2 is a schematic view showing an example of the film forming apparatus 10 when viewed from above. The A-A section in Fig. 2 is shown in Fig. 1. 3 and 4 are enlarged cross-sectional views showing an example of the left side portion of the axis X in Fig. 1. Fig. 5 is a view showing an example of the lower portion of the unit U. Fig. 6 is an enlarged cross-sectional view showing an example of a right portion of the axis X in Fig. 1. The film forming apparatus 10 shown in FIGS. 1 to 6 mainly includes a processing container 12, a mounting table 14, a first gas supply unit 16, an exhaust unit 18, a second gas supply unit 20, and a plasma generating unit 22.

如圖1所示地,處理容器12具有下部構件12a及上部構件12b。下部構件12a具有上方開口之大略筒形,且形成凹部,而該凹部包含形成處理室C之側壁及底壁。上部構件12b係具有大略筒形之蓋體,且藉由蓋封閉下部構件12a之凹部的上部開口而形成處理室C。下部構件12a與上部構件12b間之外周部設有用以密閉處理室C之彈性密封構件,例如O環。As shown in Fig. 1, the processing container 12 has a lower member 12a and an upper member 12b. The lower member 12a has a substantially cylindrical shape with an upper opening and forms a recess, and the recess includes a side wall and a bottom wall forming the process chamber C. The upper member 12b has a substantially cylindrical lid body, and the processing chamber C is formed by closing the upper opening of the recess of the lower member 12a by the lid. An outer peripheral portion between the lower member 12a and the upper member 12b is provided with an elastic sealing member for sealing the processing chamber C, for example, an O-ring.

成膜裝置10在由處理容器12形成之處理室C內部具有載置台14。載置台14係藉由驅動機構24以軸線X為中心驅動旋轉。驅動機構24具有馬達等之驅動裝置24a及旋轉軸24b,且安裝在處理容器12之下部構件12a上。The film forming apparatus 10 has a mounting table 14 inside the processing chamber C formed by the processing container 12. The mounting table 14 is driven to rotate about the axis X by the drive mechanism 24. The drive mechanism 24 has a driving device 24a of a motor or the like and a rotating shaft 24b, and is attached to the lower member 12a of the processing container 12.

旋轉軸24b係以軸線X為中心軸線,延伸至處理室C之內部。旋轉軸24b藉由從驅動裝置24a傳送之驅動力以軸線X為中心旋轉。載置台14之中央部分藉由旋轉軸24b支持。藉此,載置台14以軸線X為中心,隨著旋轉軸24b之旋轉而旋轉。此外,在處理容器12之下部構件12a與驅動機構24之間,設有密閉處理室C之例如O環等的彈性密封構件。The rotating shaft 24b extends to the inside of the processing chamber C with the axis X as a central axis. The rotating shaft 24b is rotated about the axis X by the driving force transmitted from the driving device 24a. The central portion of the stage 14 is supported by the rotating shaft 24b. Thereby, the mounting table 14 rotates with the rotation of the rotating shaft 24b centering on the axis X. Further, between the lower member 12a of the processing container 12 and the drive mechanism 24, an elastic sealing member such as an O-ring or the like that seals the processing chamber C is provided.

成膜裝置10在處理室C內部之載置台14下方,具有用以加熱基板W之加熱器26,而該基板W係載置於載置台14上之被處理基板。具體而言,加熱器26係藉由加熱載置台14來加熱基板W。The film forming apparatus 10 has a heater 26 for heating the substrate W under the mounting table 14 inside the processing chamber C, and the substrate W is a substrate to be processed placed on the mounting table 14. Specifically, the heater 26 heats the substrate W by heating the mounting table 14.

處理容器12係像例如圖2所示地,以軸線X為中心軸之大略圓筒狀容器,且內部具有處理室C。處理室C設有包含噴射部16a之單元U。處理容器12係,例如,藉由在內面實施了防蝕鋁處理或Y2 O3 (氧化釔)之熱噴塗處理等耐電漿處理的Al(鋁)等之金屬形成。成膜裝置10在處理容器12內具有多數電漿產生部22。The processing container 12 is, for example, as shown in Fig. 2, a substantially cylindrical container having an axis X as a central axis, and a processing chamber C inside. The processing chamber C is provided with a unit U including an injection portion 16a. The processing container 12 is formed of, for example, a metal such as Al (aluminum) which is subjected to plasma treatment such as alumite treatment or thermal spraying treatment of Y 2 O 3 (yttria) on the inner surface. The film forming apparatus 10 has a plurality of plasma generating portions 22 in the processing container 12.

各電漿產生部22在處理容器12之上部具有輸出微波之多數天線22a-1至22a-3。在本實施形態中,各天線22a之外形係在角具有圓形之大略三角形。在圖2中,雖然在處理容器12之上部設有3個天線22a-1至22a-3,但天線22a之數目沒有限制,可為2個以下,亦可為4個以上。Each of the plasma generating portions 22 has a plurality of antennas 22a-1 to 22a-3 for outputting microwaves on the upper portion of the processing container 12. In the present embodiment, each of the antennas 22a has a substantially triangular shape with a circular shape at an angle. In FIG. 2, although three antennas 22a-1 to 22a-3 are provided in the upper portion of the processing container 12, the number of the antennas 22a is not limited, and may be two or less, or four or more.

成膜裝置10,如例如圖2所示地,包含在上面具有多數基板載置區域14a的載置台14。載置台14係以軸線X為中心軸之大略圓板狀構件。在載置台14之上面形成有以軸線X為中心之同心圓狀多數(在圖2之例中為5個)載置基板W之基板載置區域14a。基板W配置在基板載置區域14a內,且基板載置區域14a在載置台14旋轉時支持基板W,使基板W不會位移。基板載置區域14a係與大略圓形之基板W大略同形狀的大略圓形凹部。與載置於基板載置區域14a中之基板W的直徑W1相比,基板載置區域14a之凹部的直徑大略相同。即,基板載置區域14a之凹部的直徑可使所載置之基板W嵌合於凹部,且即使載置台14旋轉,亦可固定基板W,使基板W不因離心力而由嵌合位置移動。The film forming apparatus 10 includes, for example, as shown in FIG. 2, a mounting table 14 having a plurality of substrate mounting regions 14a thereon. The mounting table 14 is a substantially disk-shaped member having a central axis X as a central axis. On the upper surface of the mounting table 14, a plurality of concentric circles (five in the example of FIG. 2) centered on the axis X are placed on the substrate mounting region 14a on which the substrate W is placed. The substrate W is disposed in the substrate mounting region 14a, and the substrate mounting region 14a supports the substrate W when the mounting table 14 rotates, so that the substrate W is not displaced. The substrate mounting region 14a is a substantially circular recess having substantially the same shape as the substantially circular substrate W. The diameter of the concave portion of the substrate mounting region 14a is substantially the same as the diameter W1 of the substrate W placed in the substrate mounting region 14a. In other words, the diameter of the concave portion of the substrate mounting region 14a allows the substrate W to be placed to be fitted into the concave portion, and even if the mounting table 14 rotates, the substrate W can be fixed, so that the substrate W is not moved by the fitting position due to the centrifugal force.

成膜裝置10在處理容器12之外緣具有用以透過機械手臂等之搬送裝置將基板W搬入處理室C,並由處理室C搬出基板W的閘閥G。此外,成膜裝置10在載置台14之外緣下方,沿載置台14之周緣具有排氣部22h。排氣部22h連接於排氣裝置52。成膜裝置10可控制排氣裝置52之動作,由排氣孔排出處理室C內之氣體,藉此將處理室C內之壓力維持在目標壓力。The film forming apparatus 10 has a gate valve G for transporting the substrate W into the processing chamber C through a transfer device such as a robot arm and carrying out the substrate W from the processing chamber C at the outer edge of the processing container 12. Further, the film forming apparatus 10 has an exhaust portion 22h along the periphery of the mounting table 14 below the outer edge of the mounting table 14. The exhaust unit 22h is connected to the exhaust unit 52. The film forming apparatus 10 can control the operation of the exhaust unit 52, and the gas in the processing chamber C is discharged from the exhaust port, thereby maintaining the pressure in the processing chamber C at the target pressure.

處理室C,如例如圖2所示地,包含排列在以軸線X為中心之圓周上的第1區域R1及第2區域R2。載置於基板載置區域14a之基板W隨著載置台14之旋轉,依序通過第1區域R1及第2區域R2。在本實施形態中,圖2所示之載置台14由上方看時以例如順時針方向旋轉。The processing chamber C includes, for example, as shown in FIG. 2, a first region R1 and a second region R2 arranged on a circumference centered on the axis X. The substrate W placed on the substrate mounting region 14a sequentially passes through the first region R1 and the second region R2 in accordance with the rotation of the mounting table 14. In the present embodiment, the mounting table 14 shown in Fig. 2 is rotated in, for example, a clockwise direction when viewed from above.

第1氣體供給部16,如例如圖3及圖4所示地,具有內側氣體供給部161、中間氣體供給部162及外側氣體供給部163。此外,在第1區域R1之上方,如例如圖3及圖4所示地,以與載置台14之上面相對之方式,設有進行氣體之供給、沖洗及排氣的單元U。單元U具有依序重疊第1構件M1、第2構件M2、第3構件M3及第4構件M4的構造。單元U以抵接在處理容器12之上部構件12b下面的方式安裝在處理容器12上。The first gas supply unit 16 includes an inner gas supply unit 161, an intermediate gas supply unit 162, and an outer air supply unit 163 as shown, for example, in FIGS. 3 and 4 . Further, above the first region R1, as shown, for example, in FIGS. 3 and 4, a unit U for supplying, flushing, and exhausting gas is provided so as to face the upper surface of the mounting table 14. The unit U has a structure in which the first member M1, the second member M2, the third member M3, and the fourth member M4 are superposed in this order. The unit U is mounted on the processing container 12 in a manner that abuts against the underlying member 12b of the processing vessel 12.

單元U,如例如圖3及圖4所示地,形成有貫穿第2構件M2至第4構件M4之氣體供給路161p、氣體供給路162p及氣體供給路163p。氣體供給路161p連接於上端設於處理容器12之上部構件12b的氣體供給路121p。氣體供給路121p透過閥161v及質量流控制器等流量控制器161c,連接於前驅物氣體之氣體供給源16g。此外,氣體供給路161p之下端連接於形成於第1構件M1與第2構件M2之間,且藉例如O環等之彈性構件161b包圍的緩衝空間161d。緩衝空間161d連接於設於第1構件M1之內側噴射部161a的噴射口16h。The unit U has a gas supply path 161p, a gas supply path 162p, and a gas supply path 163p that penetrate the second member M2 to the fourth member M4 as shown, for example, in FIGS. 3 and 4. The gas supply path 161p is connected to the gas supply path 121p provided at the upper end of the processing container 12 upper member 12b. The gas supply path 121p is connected to the gas supply source 16g of the precursor gas through the flow rate controller 161c such as the valve 161v and the mass flow controller. Further, the lower end of the gas supply path 161p is connected to a buffer space 161d formed between the first member M1 and the second member M2 and surrounded by an elastic member 161b such as an O-ring. The buffer space 161d is connected to the injection port 16h provided in the inner injection portion 161a of the first member M1.

另外,氣體供給路162p連接於上端設於處理容器12之上部構件12b的氣體供給路122p。氣體供給路122p透過閥162v及流量控制器162c,連接於氣體供給源16g。此外,氣體供給路162p之下端連接於形成於第1構件M1與第2構件M2之間,且藉例如O環等之彈性構件162b包圍的緩衝空間162d。緩衝空間162d連接於設於第1構件M1之中間噴射部162a的噴射口16h。Further, the gas supply path 162p is connected to the gas supply path 122p provided at the upper end of the processing container 12 upper member 12b. The gas supply path 122p is connected to the gas supply source 16g through the valve 162v and the flow rate controller 162c. Further, the lower end of the gas supply path 162p is connected to a buffer space 162d formed between the first member M1 and the second member M2 and surrounded by an elastic member 162b such as an O-ring. The buffer space 162d is connected to the injection port 16h provided in the intermediate injection portion 162a of the first member M1.

再者,氣體供給路163p連接於上端設於處理容器12之上部構件12b的氣體供給路123p。氣體供給路123p透過閥163v及流量控制器163c,連接於氣體供給源16g。此外,氣體供給路163p之下端連接於形成於第1構件M1與第2構件M2之間,且藉例如O環等之彈性構件163b包圍的緩衝空間163d。緩衝空間163d連接於設於第1構件M1之外側噴射部163a的噴射口16h。Further, the gas supply path 163p is connected to the gas supply path 123p provided at the upper end of the processing container 12 upper member 12b. The gas supply path 123p is connected to the gas supply source 16g through the valve 163v and the flow rate controller 163c. Further, the lower end of the gas supply path 163p is connected to a buffer space 163d formed between the first member M1 and the second member M2 and surrounded by an elastic member 163b such as an O-ring. The buffer space 163d is connected to the injection port 16h provided in the injection portion 163a on the outer side of the first member M1.

內側氣體供給部161之緩衝空間161d、中間氣體供給部162之緩衝空間162d及外側氣體供給部163之緩衝空間163d,如例如圖3及圖4所示地,形成獨立之空間。而且,通過各緩衝空間之前驅物氣體流量可分別藉由流量控制器161c、流量控制器162c及流量控制器163c獨立地控制。The buffer space 161d of the inner gas supply unit 161, the buffer space 162d of the intermediate gas supply unit 162, and the buffer space 163d of the outer air supply unit 163 form an independent space as shown, for example, in FIGS. 3 and 4 . Moreover, the precursor gas flow rate through each buffer space can be independently controlled by the flow rate controller 161c, the flow rate controller 162c, and the flow rate controller 163c.

在單元U中,如例如圖3及圖4所示地,形成有貫穿第4構件M4之氣體供給路20r。氣體供給路20r連接於上端設於處理容器12之上部構件12b的氣體供給路12r。氣體供給路12r透過閥20v及流量控制器20c,連接於沖洗氣體之氣體供給源20g。In the unit U, as shown, for example, in FIGS. 3 and 4, a gas supply path 20r penetrating through the fourth member M4 is formed. The gas supply path 20r is connected to the gas supply path 12r provided at the upper end of the processing container 12 upper member 12b. The gas supply path 12r is connected to the gas supply source 20g of the flushing gas through the valve 20v and the flow rate controller 20c.

氣體供給路20r之下端連接於設在第4構件M4之下面與第3構件M3之上面間的空間20d。此外,第4構件M4形成收容第1構件M1至第3構件M3之凹部。形成凹部之第4構件M4的內側面與第3構件M3之外側面間設有間隙20p。間隙20p連接於空間20d。間隙20p之下端具有作為噴射口20a之機能。The lower end of the gas supply path 20r is connected to a space 20d provided between the lower surface of the fourth member M4 and the upper surface of the third member M3. Further, the fourth member M4 forms a recess in which the first member M1 to the third member M3 are housed. A gap 20p is provided between the inner surface of the fourth member M4 forming the recess and the outer surface of the third member M3. The gap 20p is connected to the space 20d. The lower end of the gap 20p has a function as the ejection port 20a.

在單元U中,如例如圖3及圖4所示地,形成貫穿第3構件M3及第4構件M4之排氣路18q。排氣路18q與上端設於處理容器12之上部構件12b的排氣路12q連接。排氣路12q連接於真空泵等之排氣裝置34。此外,排氣路18q下端連接於設在第3構件M3之下面與第2構件M2之上面間的空間18d。In the unit U, as shown, for example, in FIGS. 3 and 4, an exhaust passage 18q penetrating the third member M3 and the fourth member M4 is formed. The exhaust passage 18q is connected to an exhaust passage 12q whose upper end is provided in the upper member 12b of the processing container 12. The exhaust passage 12q is connected to an exhaust device 34 such as a vacuum pump. Further, the lower end of the exhaust passage 18q is connected to a space 18d provided between the lower surface of the third member M3 and the upper surface of the second member M2.

第3構件M3具有收容第1構件M1及第2構件M2之凹部。在構成第3構件M3具有之凹部的第3構件M3內側面與第1構件M1及第2構件M2之外側面間,設有間隙18g。空間18d連接於間隙18g。間隙18g之下端具有作為排氣口18a之機能。The third member M3 has a concave portion that accommodates the first member M1 and the second member M2. A gap 18g is provided between the inner surface of the third member M3 constituting the recessed portion of the third member M3 and the outer surface of the first member M1 and the second member M2. The space 18d is connected to the gap 18g. The lower end of the gap 18g has a function as the exhaust port 18a.

在單元U之下面,即,與載置台14對向之面上,如例如圖5所示,沿遠離軸線X之方向的Y軸方向設有噴射部16a。在處理室C包含之區域中在噴射部16a對面的區域係第1區域R1。噴射部16a朝載置台14上之基板W噴射前驅物氣體。噴射部16a,如例如圖5所示,具有內側噴射部161a、中間噴射部162a及外側噴射部163a。Below the unit U, that is, on the surface facing the mounting table 14, as shown, for example, in Fig. 5, the injection portion 16a is provided in the Y-axis direction away from the axis X. The region opposite to the ejection portion 16a in the region included in the processing chamber C is the first region R1. The ejection portion 16a ejects the precursor gas toward the substrate W on the mounting table 14. As shown, for example, in FIG. 5, the injection portion 16a has an inner injection portion 161a, an intermediate injection portion 162a, and an outer injection portion 163a.

內側噴射部161a,如例如圖5所示,形成於相對軸線X之距離為r1至r2之範圍內的環狀區域中,單元U之下面所包含區域的內側環狀區域A1內。此外,中間噴射部162a形成於相對軸線X之距離為r2至r3之範圍內的環狀區域中,單元U之下面所包含區域的中間環狀區域A2內。另外,外側噴射部163a形成於相對軸線X之距離為r3至r4之範圍內的環狀區域中,單元U之下面所包含區域的外側環狀區域A3內。The inner spray portion 161a is formed in the inner annular region A1 of the region included in the lower surface of the unit U in an annular region having a distance from the axis X to r1 to r2 as shown, for example, in FIG. 5. Further, the intermediate injection portion 162a is formed in the annular region in the range of r2 to r3 with respect to the axis X, and the intermediate annular region A2 of the region included in the lower portion of the unit U. Further, the outer injection portion 163a is formed in an annular region within a range of r3 to r4 with respect to the axis X, and is located in the outer annular region A3 of the region included in the lower surface of the unit U.

形成於單元U之下面的噴射部16a在沿Y軸方向延伸之範圍內由r1到r4的長度L,如例如圖5所示,相較於直徑W1之基板W通過Y軸的長度,在軸線X側之方向上長預定距離DL以上,且在與軸線X側相反之方向上長預定距離DL以上。The ejection portion 16a formed under the unit U has a length L of r1 to r4 in a range extending in the Y-axis direction, as shown, for example, in FIG. 5, the length of the substrate W passing through the Y-axis compared to the diameter W1, on the axis The direction of the X side is longer than the predetermined distance DL, and is longer than the predetermined distance DL in the direction opposite to the side of the axis X.

內側噴射部161a、中間噴射部162a及外側噴射部163a,如例如圖5所示,具有多數噴射口16h。前驅物氣體由各噴射口16h朝第1區域R1噴射。由內側噴射部161a、中間噴射部162a及外側噴射部163a之各噴射口16h朝第1區域R1噴射的前驅物氣體流量分別藉由流量控制器161c、流量控制器162c及流量控制器163c獨立地控制。藉由供給前驅物氣體至第1區域R1,前驅物氣體之原子或分子吸附在通過第1區域R1之基板W的表面上。前驅物氣體使用含有氮原子之氣體;包含例如DCS(二氯矽烷)、單氯矽烷、三氯矽烷及六氯矽烷等之氣體。The inner injection portion 161a, the intermediate injection portion 162a, and the outer injection portion 163a have a plurality of injection ports 16h as shown, for example, in FIG. The precursor gas is ejected toward the first region R1 by the respective ejection ports 16h. The flow rate of the precursor gas injected into the first region R1 by the respective injection ports 16h of the inner injection portion 161a, the intermediate injection portion 162a, and the outer injection portion 163a is independently generated by the flow rate controller 161c, the flow rate controller 162c, and the flow rate controller 163c. control. By supplying the precursor gas to the first region R1, atoms or molecules of the precursor gas are adsorbed on the surface of the substrate W passing through the first region R1. The precursor gas uses a gas containing a nitrogen atom; and contains a gas such as DCS (dichlorodecane), monochlorodecane, trichlorodecane, and hexachlorodecane.

在第1區域R1之上方,如例如圖3及圖4所示地,以與載置台14之上面相對的方式,設有排氣部18之排氣口18a。排氣口18a,如例如圖5所示地,以包圍噴射部16a之周圍的方式,形成於單元U之下面。排氣口18a,藉由真空泵等之排氣裝置34的動作,透過排氣口18a使處理室C內之氣體排氣。Above the first region R1, as shown, for example, in FIGS. 3 and 4, an exhaust port 18a of the exhaust portion 18 is provided so as to face the upper surface of the mounting table 14. The exhaust port 18a is formed below the unit U so as to surround the periphery of the injection portion 16a as shown, for example, in FIG. The exhaust port 18a exhausts the gas in the processing chamber C through the exhaust port 18a by the operation of the exhaust device 34 such as a vacuum pump.

在第1區域R1之上方,如例如圖3及圖4所示地,以與載置台14之上面相對的方式,設有第2氣體供給部20之噴射口20a。噴射口20a,如例如圖5所示地,以包圍排氣口18a之周圍的方式,形成於單元U之下面。第2氣體供給部20透過噴射口20a朝第1區域R1噴射沖洗氣體。藉由第2氣體供給部20噴射之沖洗氣體係例如Ar(氬)等之惰性氣體。藉由噴射沖洗氣體至基板W之表面,可由基板W去除過剩地吸附在基板W上之前驅物氣體的原子或分子(殘留氣體成分)。藉此,在基板W之表面可形成吸附了前驅物氣體之原子或分子的原子層或分子層。Above the first region R1, as shown, for example, in FIGS. 3 and 4, the injection port 20a of the second gas supply unit 20 is provided so as to face the upper surface of the mounting table 14. The injection port 20a is formed below the unit U so as to surround the periphery of the exhaust port 18a as shown, for example, in FIG. The second gas supply unit 20 injects the flushing gas into the first region R1 through the injection port 20a. The flushing gas system jetted by the second gas supply unit 20 is an inert gas such as Ar (argon). By spraying the flushing gas onto the surface of the substrate W, atoms or molecules (residual gas components) of the precursor gas excessively adsorbed on the substrate W can be removed from the substrate W. Thereby, an atomic layer or a molecular layer in which atoms or molecules of the precursor gas are adsorbed can be formed on the surface of the substrate W.

單元U由噴射口20a噴射沖洗氣體,且使沖洗氣體由排氣口18a沿載置台14之表面排氣。藉此,單元U可抑制供給至第1區域R1之前驅物氣體漏出第1區域R1外。此外,由於單元U由噴射口20a噴射沖洗氣體並使沖洗氣體由排氣口18a沿載置台14之面排氣,可抑制供給至第2區域R2之反應氣體或反應氣體之自由基等侵入至第1區域R1內。即,單元U藉由從第2氣體供給部20噴射沖洗氣體及從排氣部18排氣,可使第1區域R1與第2區域R2分離。The unit U injects the flushing gas from the injection port 20a, and exhausts the flushing gas from the surface of the mounting table 14 by the exhaust port 18a. Thereby, the unit U can suppress the leakage of the exchanging gas outside the first region R1 before being supplied to the first region R1. Further, since the unit U injects the flushing gas from the injection port 20a and exhausts the flushing gas from the surface of the mounting table 14 by the exhaust port 18a, it is possible to suppress the intrusion of radicals or reaction gases such as the reaction gas or the reaction gas supplied to the second region R2. In the first area R1. In other words, the unit U can separate the first region R1 from the second region R2 by injecting the flushing gas from the second gas supply unit 20 and exhausting it from the exhaust unit 18.

成膜裝置10,如例如圖6所示地,在第2區域R2上方之上部構件12b的開口AP,具有設置成與載置台14之上面相對的電漿產生部22。電漿產生部22具有天線22a、供給微波至天線22a之同軸波導管22b、及供給反應氣體至第2區域R2之反應氣體供給部22c。在本實施形態中,在上部構件12b形成有例如3個開口AP,且成膜裝置10具有例如3個天線22a-1至22a-3。As shown in, for example, FIG. 6, the film forming apparatus 10 has a plasma generating portion 22 that is disposed to face the upper surface of the mounting table 14 in the opening AP of the upper member 12b above the second region R2. The plasma generating unit 22 includes an antenna 22a, a coaxial waveguide 22b that supplies microwaves to the antenna 22a, and a reaction gas supply unit 22c that supplies a reaction gas to the second region R2. In the present embodiment, for example, three openings AP are formed in the upper member 12b, and the film forming apparatus 10 has, for example, three antennas 22a-1 to 22a-3.

電漿產生部22由天線22a及同軸波導管22b供給微波至第2區域R2,並由反應氣體供給部22c供應反應氣體至第2區域R2,藉此在第2區域R2中產生反應氣體之電漿。而且,對吸附在基板W表面上之原子層或分子層實施電漿處理。在本實施形態中,反應氣體使用含氮原子氣體時,電漿產生部22使吸附在基板W上之原子層或分子層氮化。反應氣體可使用例如N2 (氮)氣體與H2 (氫)氣體之混合氣體、或NH3 (氨)氣體與H2 (氫)氣體之混合氣體等的含氮原子氣體。The plasma generating unit 22 supplies microwaves to the second region R2 by the antenna 22a and the coaxial waveguide 22b, and supplies the reaction gas to the second region R2 by the reaction gas supply unit 22c, thereby generating electricity of the reaction gas in the second region R2. Pulp. Further, a plasma treatment is performed on the atomic layer or the molecular layer adsorbed on the surface of the substrate W. In the present embodiment, when a nitrogen-containing gas is used as the reaction gas, the plasma generating unit 22 nitrides the atomic layer or the molecular layer adsorbed on the substrate W. As the reaction gas, for example, a mixed gas of a N 2 (nitrogen) gas and a H 2 (hydrogen) gas, or a nitrogen atom-containing gas such as a mixed gas of NH 3 (ammonia) gas and H 2 (hydrogen) gas can be used.

電漿產生部22,如例如圖6所示地,以閉塞開口AP之方式氣密地配置天線22a。天線22a具有頂板40、開槽板42及慢波板44。頂板40係藉介電體形成之圓角大略正三角形構件,且由例如氧化鋁陶瓷等形成。頂板40藉由上部構件12b支持,使其下面由形成於處理容器12之上部構件12b的開口AP露出第2區域R2。The plasma generating unit 22 hermetically arranges the antenna 22a so as to close the opening AP as shown, for example, in FIG. The antenna 22a has a top plate 40, a slotted plate 42, and a slow wave plate 44. The top plate 40 is a rounded substantially triangular member formed of a dielectric body, and is formed of, for example, alumina ceramics or the like. The top plate 40 is supported by the upper member 12b such that the lower portion thereof is exposed to the second region R2 by the opening AP formed in the upper member 12b of the processing container 12.

開槽板42設在頂板40之上面。開槽板42係形成大略正三角形之板狀金屬製構件。在開槽板42中形成有多數槽孔對。各槽孔對包含互相直交的2個槽孔。The slotted plate 42 is disposed above the top plate 40. The slotted plate 42 is formed of a plate-like metal member having a substantially equilateral triangle shape. A plurality of slot pairs are formed in the slotted plate 42. Each slot pair includes two slots that are orthogonal to each other.

慢波板44設在開槽板42之上面。慢波板44係藉由例如氧化鋁陶瓷等之介電體,形成大略正三角形。慢波板44設有用以配置同軸波導管22b之外側導體62b的大略圓筒狀開口。The slow wave plate 44 is disposed above the grooved plate 42. The slow wave plate 44 is formed into a substantially regular triangle by a dielectric such as alumina ceramic. The slow wave plate 44 is provided with a substantially cylindrical opening for arranging the outer side conductor 62b of the coaxial waveguide 22b.

金屬製之冷卻板46設在慢波板44之上面。冷卻板46藉由流通形成於其內部之流路的冷媒,可透過慢波板44來冷卻天線22a。冷卻板46藉由未圖示之彈簧等推壓慢波板44之上面,使冷卻板46之下面密接在慢波板44之上面。A metal cooling plate 46 is disposed above the slow wave plate 44. The cooling plate 46 can pass through the slow wave plate 44 to cool the antenna 22a by circulating a refrigerant flowing through the flow path formed therein. The cooling plate 46 presses the upper surface of the slow wave plate 44 by a spring or the like (not shown) so that the lower surface of the cooling plate 46 is in close contact with the upper surface of the slow wave plate 44.

同軸波導管22b具有內側導體62a及外側導體62b。內側導體62a由天線22a之上方貫穿慢波板44之開口及開槽板42之開口。外側導體62b在內側導體62a之外周面與外側導體62b之內周面之間具有間隙,並設置成包圍內側導體62a。外側導體62b之下端連接於冷卻板46之開口部。此外,天線22a可具有作為電極之機能。或者,亦可使用設於處理容器12內之電極作為天線22a。The coaxial waveguide 22b has an inner conductor 62a and an outer conductor 62b. The inner conductor 62a penetrates the opening of the slow wave plate 44 and the opening of the grooved plate 42 from above the antenna 22a. The outer conductor 62b has a gap between the outer peripheral surface of the inner conductor 62a and the inner peripheral surface of the outer conductor 62b, and is provided to surround the inner conductor 62a. The lower end of the outer conductor 62b is connected to the opening of the cooling plate 46. Further, the antenna 22a may have a function as an electrode. Alternatively, an electrode provided in the processing container 12 may be used as the antenna 22a.

成膜裝置10具有波導管60及微波產生器68。微波產生器68產生之例如大約2.45GHz的微波透過波導管60傳送至同軸波導管22b,並傳送通過內側導體62a與外側導體62b之間隙。而且,傳送通過慢波板44內之微波由開槽板42之槽孔傳送至頂板40,並由頂板40朝第2區域R2發射。The film forming apparatus 10 has a waveguide 60 and a microwave generator 68. The microwave generated by the microwave generator 68, for example, about 2.45 GHz, is transmitted through the waveguide 60 to the coaxial waveguide 22b and through the gap between the inner conductor 62a and the outer conductor 62b. Further, the microwaves transmitted through the slow wave plate 44 are transferred from the slots of the slotted plate 42 to the top plate 40, and are emitted from the top plate 40 toward the second region R2.

反應氣體由反應氣體供給部22c供給至第2區域R2。反應氣體供給部22c,如例如圖2所示地具有多數內側噴射部50b及多數外側噴射口51b。各內側噴射口50b,如例如圖6所示地,透過閥50v及質量流控制器等之流量控制部50c連接於反應氣體之氣體供給源50g。各內側噴射口50b,如例如圖6所示地,設於處理容器12之上部構件12b的下面。The reaction gas is supplied from the reaction gas supply unit 22c to the second region R2. The reaction gas supply unit 22c has a plurality of inner injection portions 50b and a plurality of outer injection ports 51b as shown, for example, in Fig. 2 . Each of the inner injection ports 50b is connected to the gas supply source 50g of the reaction gas through the flow rate control unit 50c such as the permeation valve 50v and the mass flow controller, as shown, for example. Each of the inner injection ports 50b is provided on the lower surface of the upper member 12b of the processing container 12 as shown, for example, in FIG.

各內側噴射口50b將透過閥50v及流量控制部50c由氣體供給源50g供給之反應氣體,沿遠離軸線X之方向,例如,朝向與載置於載置台14之基板載置區域14a的基板W面平行的方向,噴射至天線22a下方之第2區域R2。Each of the inside injection ports 50b supplies the reaction gas supplied from the gas supply source 50g through the valve 50v and the flow rate control unit 50c in a direction away from the axis X, for example, toward the substrate W placed on the substrate mounting region 14a of the mounting table 14. The plane parallel to the surface is ejected to the second region R2 below the antenna 22a.

各外側噴射口51b透過閥51v及質量流控制器等之流量控制部51c連接於反應氣體之氣體供給源50g。各外側噴射口51b,如例如圖6所示地,設於處理容器12之上部構件12b的下面。各內側噴射口51b將透過閥51v及流量控制部51c由氣體供給源50g供給之反應氣體,沿接近軸線X之方向噴射,例如,沿與載置於載置台14之基板載置區域14a的基板W面平行的方向噴射反應氣體。Each of the outer injection ports 51b is connected to the gas supply source 50g of the reaction gas through the flow rate control unit 51c such as the valve 51v and the mass flow controller. Each of the outer injection ports 51b is provided on the lower surface of the upper member 12b of the processing container 12 as shown, for example, in FIG. Each of the inside injection ports 51b ejects the reaction gas supplied from the gas supply source 50g through the valve 51v and the flow rate control unit 51c in the direction of the axis X, for example, along the substrate placed on the substrate mounting region 14a of the mounting table 14. The reaction gas is sprayed in a direction parallel to the W plane.

此外,在本實施形態中,由內側噴射口50b及外側噴射口51b噴射之反應氣體的流量係分別藉由流量控制部50c及流量控制部51c獨立地控制。另外,流量控制部50c及流量控制部51c可設於每一天線22a上,亦可由每一天線22a獨立地控制由內側噴射口50b及外側噴射口51b噴射之反應氣體的流量。Further, in the present embodiment, the flow rates of the reaction gases injected from the inner injection port 50b and the outer injection port 51b are independently controlled by the flow rate control unit 50c and the flow rate control unit 51c. Further, the flow rate control unit 50c and the flow rate control unit 51c may be provided on each of the antennas 22a, and the flow rate of the reaction gas injected from the inner injection port 50b and the outer injection port 51b may be independently controlled by each antenna 22a.

電漿產生部22藉由多數內側噴射口50b及多數外側噴射口51b供給反應氣體至第2區域R2,並藉由天線22a發射微波至第2區域R2。藉此,電漿產生部22可在第2區域R2中產生反應氣體之電漿。The plasma generating unit 22 supplies the reaction gas to the second region R2 via the plurality of inner injection ports 50b and the plurality of outer injection ports 51b, and emits microwaves to the second region R2 via the antenna 22a. Thereby, the plasma generating unit 22 can generate a plasma of the reaction gas in the second region R2.

在載置台14之周緣,如例如圖2所示地,設有排氣部22h。排氣部22h,如例如圖6所示地,具有上部開口之溝部222及設於溝部222上部之蓋部221。溝部222連接於排氣裝置52。蓋部221在例如圖2所示之排氣區域220h中具有多數排氣孔。On the periphery of the mounting table 14, as shown, for example, in Fig. 2, an exhaust portion 22h is provided. The exhaust portion 22h has a groove portion 222 having an upper opening and a lid portion 221 provided at an upper portion of the groove portion 222, as shown, for example, in FIG. The groove portion 222 is connected to the exhaust device 52. The cover portion 221 has a plurality of exhaust holes in, for example, the exhaust region 220h shown in FIG.

此外,在外側噴射口51b之下方,蓋部221上設有分隔件220。分隔件220,如例如圖6所示地,具有與蓋部221之上面到載置台14之上面的高度大略相同之厚度。分隔件220可抑制在外側噴射口51b之下方,因載置台14與蓋部221之段差產生之氣體流速的增加。Further, below the outer injection port 51b, a partition 220 is provided on the lid portion 221. The separator 220 has a thickness substantially equal to the height of the upper surface of the lid portion 221 to the upper surface of the mounting table 14, as shown, for example, in FIG. The partition member 220 can suppress an increase in the flow velocity of the gas generated by the step of the mounting table 14 and the lid portion 221 below the outer injection port 51b.

排氣部22h在各排氣區域220h中,藉由排氣裝置52之動作,由設於蓋部221之多數排氣孔透過溝部222使處理室C內之氣體排氣。此外,可調整設於各排氣區域220h之排氣孔的位置、大小及數目,使設於蓋部221之排氣孔的來自各排氣區域220h之排氣量大略相同。In each of the exhaust regions 220h, the exhaust portion 22h exhausts the gas in the processing chamber C by the plurality of exhaust holes provided in the lid portion 221 through the groove portion 222 by the operation of the exhaust device 52. Further, the position, size, and number of the exhaust holes provided in each of the exhaust regions 220h can be adjusted, and the amount of exhaust gas from each of the exhaust regions 220h provided in the exhaust holes of the cover portion 221 is substantially the same.

成膜裝置10,如例如圖1所示地,具有用以控制成膜裝置10之各構成元件的控制部70。控制部70可為具有CPU(中央處理單元;Central Processing Unit)等之控制裝置、記憶體等之記憶裝置、輸出輸入裝置等的電腦。控制部70藉由依據記憶於記憶體之控制程式使CPU動作,控制成膜裝置10之各構成元件。The film forming apparatus 10 has a control unit 70 for controlling each constituent element of the film forming apparatus 10 as shown, for example, in FIG. The control unit 70 may be a computer having a control device such as a CPU (Central Processing Unit), a memory device such as a memory, and an output input device. The control unit 70 controls the constituent elements of the film forming apparatus 10 by operating the CPU in accordance with a control program stored in the memory.

控制部70發送控制載置台14之旋轉速度的控制信號至驅動裝置24a。此外,控制部70發送控制基板W溫度之控制信號至連接於加熱器26之電源。另外,控制部70發送控制前驅物氣體流量之控制信號至閥161v至163v及流量控制器161c至163c。再者,控制部70發送控制連接於排氣口18a之排氣裝置34之排氣量的控制信號至排氣裝置34。The control unit 70 transmits a control signal for controlling the rotational speed of the mounting table 14 to the drive device 24a. Further, the control unit 70 transmits a control signal for controlling the temperature of the substrate W to a power source connected to the heater 26. Further, the control unit 70 transmits a control signal for controlling the flow rate of the precursor gas to the valves 161v to 163v and the flow rate controllers 161c to 163c. Further, the control unit 70 transmits a control signal for controlling the amount of exhaust of the exhaust unit 34 connected to the exhaust port 18a to the exhaust unit 34.

此外,控制部70發送控制沖洗氣體流量之控制信號至閥20v及流量控制器20c。另外,控制部70發送控制微波之發送功率的控制信號至微波產生器68。再者,控制部70發送控制反應氣體流量之控制信號至閥50v、閥51v、流量控制部50c及流量控制部51c。此外,控制部70發送控制來自排氣部22h之排氣量的控制信號至排氣裝置52。Further, the control unit 70 transmits a control signal for controlling the flow rate of the flushing gas to the valve 20v and the flow rate controller 20c. Further, the control unit 70 transmits a control signal for controlling the transmission power of the microwave to the microwave generator 68. Further, the control unit 70 transmits a control signal for controlling the flow rate of the reaction gas to the valve 50v, the valve 51v, the flow rate control unit 50c, and the flow rate control unit 51c. Further, the control unit 70 transmits a control signal for controlling the amount of exhaust gas from the exhaust unit 22h to the exhaust unit 52.

藉由如上所述地構成之成膜裝置10,由第1氣體供給部16噴射前驅物氣體至藉由載置台14之旋轉而移動的基板W上,並藉由排氣部18及第2氣體供給部20由基板W去除過剩地吸附之前驅物氣體。然後,藉由載置台14之旋轉而移動的基板W暴露於藉由電漿產生部22產生之反應氣體的電漿中。藉由載置台14之旋轉,對基板W重複進行上述動作,成膜裝置10可在基板W上形成預定厚度之膜。 [實施例]According to the film forming apparatus 10 configured as described above, the precursor gas is ejected from the first gas supply unit 16 to the substrate W that is moved by the rotation of the mounting table 14, and the exhaust portion 18 and the second gas are used. The supply unit 20 removes excessively adsorbed precursor gas from the substrate W. Then, the substrate W moved by the rotation of the mounting table 14 is exposed to the plasma of the reaction gas generated by the plasma generating portion 22. The above operation is repeated on the substrate W by the rotation of the mounting table 14, and the film forming apparatus 10 can form a film of a predetermined thickness on the substrate W. [Examples]

以下,使用利用圖1至圖6說明之成膜裝置10,進行在含有碳原子之基底膜上,形成厚度例如大約20nm之SiN膜作為氮化膜,並在SiN膜上藉由蒸鍍例如鉑等形成導體膜的實驗。基底膜係含碳膜之一例。Hereinafter, using the film forming apparatus 10 described with reference to FIGS. 1 to 6, a SiN film having a thickness of, for example, about 20 nm is formed as a nitride film on a base film containing carbon atoms, and a platinum such as platinum is deposited on the SiN film. An experiment to form a conductor film. An example of a carbon film containing a basement membrane.

首先,進行使用DCS作為前驅物氣體,並使用NH3 氣體及H2 氣體之混合氣體作為反應氣體,在基底膜上形成SiN膜的實驗。NH3 氣體係包含氫原子之氮化物氣體的一例。圖7A係顯示進行成膜處理前之基板W剖面之一例的示意圖。圖7B係顯示使用NH3 氣體及H2 氣體之混合氣體進行成膜處理時基板W剖面之一例的示意圖。First, an experiment in which a DCN was used as a precursor gas and a mixed gas of NH 3 gas and H 2 gas was used as a reaction gas to form a SiN film on a base film was performed. An example of a nitride gas containing a hydrogen atom in the NH 3 gas system. Fig. 7A is a schematic view showing an example of a cross section of a substrate W before performing a film formation process. Fig. 7B is a schematic view showing an example of a cross section of a substrate W when a film forming process is performed using a mixed gas of NH 3 gas and H 2 gas.

在本實驗之SiN膜的成膜處理中,如圖7A所示地,使用在矽等之基底基板100上形成有厚度大約60nm之含有碳原子之基底膜101的基板W。使用NH3 氣體及H2 氣體之混合氣體作為反應氣體進行成膜處理時,如圖7B所示地,未在基底膜101上形成SiN膜。此外,如圖7B所示地,成膜處理後之基底膜101的厚度減少至大約25nm,且在內部亦產生空隙。這是因為反應氣體之電漿包含的氫原子與基底膜101包含之碳原子反應,使基底膜101分解。In the film formation process of the SiN film of the present experiment, as shown in FIG. 7A, a substrate W having a base film 101 containing carbon atoms having a thickness of about 60 nm formed on a base substrate 100 of ruthenium or the like is used. When a film formation process is performed using a mixed gas of NH 3 gas and H 2 gas as a reaction gas, as shown in FIG. 7B, an SiN film is not formed on the base film 101. Further, as shown in Fig. 7B, the thickness of the base film 101 after the film formation treatment is reduced to about 25 nm, and voids are also generated inside. This is because the hydrogen atoms contained in the plasma of the reaction gas react with the carbon atoms contained in the base film 101 to decompose the base film 101.

接著,進行使用DCS作為前驅物氣體,並只使用NH3 氣體作為反應氣體,在基底膜上形成SiN膜的實驗。圖8A係顯示進行成膜處理前之基板W剖面之一例的示意圖。圖8B係顯示使用NH3 氣體進行成膜處理時基板W剖面之一例的示意圖。Next, an experiment of forming a SiN film on the base film using DCS as a precursor gas and using only NH 3 gas as a reaction gas was performed. Fig. 8A is a schematic view showing an example of a cross section of a substrate W before performing a film formation process. Fig. 8B is a schematic view showing an example of a cross section of a substrate W when a film formation process is performed using NH 3 gas.

在本實驗之SiN膜的成膜處理中,如圖8A所示地,使用在基底基板100上形成有厚度大約62.4nm之基底膜101的基板W。此外,前驅物氣體使用DCS。只使用NH3 氣體作為反應氣體進行成膜處理時,如圖8B所示地,可在基底膜101上形成厚度大約17.8nm之SiN膜102。由於形成了SiN膜102,在SiN膜102上形成導體膜103。In the film formation process of the SiN film of the present experiment, as shown in FIG. 8A, the substrate W on which the base film 101 having a thickness of about 62.4 nm was formed on the base substrate 100 was used. In addition, the precursor gas uses DCS. When the film formation process is performed using only NH 3 gas as the reaction gas, as shown in FIG. 8B, the SiN film 102 having a thickness of about 17.8 nm can be formed on the base film 101. Since the SiN film 102 is formed, the conductor film 103 is formed on the SiN film 102.

但是,如圖8B所示地,成膜處理後之基底膜101的厚度由大約62.4nm大幅減少至大約23.6nm,且在基底膜101內部亦產生空隙。此外,基底膜101與基底基板100之間亦發現空隙。因此,基底膜101與基底基板100之密接力降低,基底膜101容易由基底基板100剝離。However, as shown in FIG. 8B, the thickness of the base film 101 after the film formation treatment is greatly reduced from about 62.4 nm to about 23.6 nm, and voids are also generated inside the base film 101. Further, a void is also found between the base film 101 and the base substrate 100. Therefore, the adhesion between the base film 101 and the base substrate 100 is lowered, and the base film 101 is easily peeled off from the base substrate 100.

這是因為NH3 氣體中亦包含氫原子,故NH3 氣體之電漿包含的氫原子與基底膜101包含之碳原子反應,使基底膜101分解。因此,只使用NH3 氣體作為反應氣體時,雖然可在含有碳原子之基底膜101上形成SiN膜102,但會減少基底膜101之膜厚或產生空隙等,對基底膜101造成嚴重破壞。This is because the NH 3 gas also contains hydrogen atoms, so that the hydrogen atoms contained in the plasma of the NH 3 gas react with the carbon atoms contained in the base film 101 to decompose the base film 101. Therefore, when only the NH 3 gas is used as the reaction gas, the SiN film 102 can be formed on the base film 101 containing carbon atoms, but the film thickness of the base film 101 or voids are reduced, and the base film 101 is severely damaged.

接著,進行使用DCS作為前驅物氣體,並使用N2 氣體及惰性氣體之混合氣體作為反應氣體,在基底膜上形成SiN膜的實驗。N2 氣體係不含氫原子之氮化物氣體的一例。在本實驗中,使用Ar氣體作為惰性氣體。此外,前驅物氣體使用DCS。圖9係顯示使用N2 氣體及Ar氣體之混合氣體進行成膜處理時基板W剖面之一例的示意圖。Next, an experiment was conducted in which a SiN film was formed on a base film by using DCS as a precursor gas and using a mixed gas of N 2 gas and an inert gas as a reaction gas. An example of a nitride gas containing no hydrogen atoms in the N 2 gas system. In this experiment, Ar gas was used as an inert gas. In addition, the precursor gas uses DCS. FIG. 9 is a schematic view showing an example of a cross section of a substrate W when a film formation process is performed using a mixed gas of N 2 gas and Ar gas.

在本實驗之SiN膜的成膜處理中,與圖8A所示之基板W同樣地,使用形成有大約62.4nm之基底膜101的基板W。使用N2 氣體及Ar氣體之混合氣體進行成膜處理時,如圖9所示地,可在基底膜101上形成厚度大約20.1nm之SiN膜102。由於形成了SiN膜102,在SiN膜102上形成導體膜103。In the film formation process of the SiN film of the present experiment, a substrate W on which the base film 101 of about 62.4 nm was formed was used in the same manner as the substrate W shown in FIG. 8A. When a film formation process is performed using a mixed gas of N 2 gas and Ar gas, as shown in FIG. 9, an SiN film 102 having a thickness of about 20.1 nm can be formed on the base film 101. Since the SiN film 102 is formed, the conductor film 103 is formed on the SiN film 102.

在本實驗中,如圖9所示地,雖然成膜處理後之基底膜101的厚度由大約62.4nm減少至大約55.4nm,但相較於使用NH3 氣體及H2 氣體之混合氣體進行成膜處理時,或只使用NH3 氣體進行成膜處理時的基底膜101,膜厚之減少量小得多。此外,在本實驗中,在基底膜101內部未發現空隙。另外,基底膜101與基底基板100之間亦未發現空隙,可考慮亦維持基底膜101與基底基板100之密接力。In the present experiment, as shown in FIG. 9, although the thickness of the base film 101 after the film formation treatment was reduced from about 62.4 nm to about 55.4 nm, it was formed in comparison with a mixed gas using NH 3 gas and H 2 gas. In the film treatment, or in the base film 101 in which the film formation treatment is performed using only NH 3 gas, the amount of film thickness reduction is much smaller. Further, in the present experiment, no void was found inside the base film 101. Further, no void is found between the base film 101 and the base substrate 100, and it is conceivable to maintain the adhesion between the base film 101 and the base substrate 100.

可了解的是藉由使用N2 氣體及Ar氣體之混合氣體作為反應氣體,可在基底膜101上形成SiN膜102,同時可抑制減少基底膜101之膜厚或產生空隙等對基底膜101之破壞。接著,進行改變N2 氣體及Ar氣體之流量比的實驗,檢討可抑制減少基底膜101之膜厚或產生空隙等之破壞的條件範圍。It is understood that the SiN film 102 can be formed on the base film 101 by using a mixed gas of N 2 gas and Ar gas as a reaction gas, and at the same time, it is possible to suppress the film thickness of the base film 101 or to generate voids and the like to the base film 101. damage. Then, an experiment of changing the flow ratio of the N 2 gas and the Ar gas is performed, and the range of conditions for suppressing the reduction of the film thickness of the underlying film 101 or the occurrence of voids or the like is examined.

圖10A至圖10D係顯示改變N2 氣體及Ar氣體之流量比進行成膜處理時之基板W剖面之一例的示意圖。此外,在圖10A至圖10D所示之實驗中,與圖8A所示之基板W同樣地,使用形成有大約62.4nm之基底膜101的基板W。另外,使用DCS作為前驅物氣體。再者,在圖10A至圖10D所示之實驗中,電漿處理中之基板W的溫度係300℃,且使用供給微波之天線22a-2及22a-3,由各天線22a供給之微波功率係4.0kW,且載置台14之旋轉速度係20rpm。10A to 10D are schematic views showing an example of a cross section of a substrate W when a flow ratio of N 2 gas and Ar gas is changed to perform a film formation process. Further, in the experiment shown in FIGS. 10A to 10D, similarly to the substrate W shown in FIG. 8A, the substrate W on which the base film 101 of about 62.4 nm was formed was used. In addition, DCS was used as the precursor gas. Further, in the experiments shown in Figs. 10A to 10D, the temperature of the substrate W in the plasma processing was 300 ° C, and the microwave power supplied from each antenna 22a was used using the antennas 22a-2 and 22a-3 for supplying microwaves. It is 4.0 kW, and the rotation speed of the mounting table 14 is 20 rpm.

圖10A係顯示使用N2 氣體/Ar氣體=20/5000sccm之流量比的反應氣體進行成膜處理時基板剖面之一例的示意圖。圖10A所示之實驗結果係可在基底膜101上形成厚度大約18.6nm之SiN膜102。此外,圖10A所示之實驗結果中,雖然成膜處理後之基底膜101的厚度由大約62.4nm減少至大約52.3nm,但膜厚之減少量小。另外,在本實驗中,在基底膜101內部未發現空隙,且基底膜101與基底基板100之間亦未發現空隙。Fig. 10A is a schematic view showing an example of a cross section of a substrate when a film formation process is performed using a reaction gas having a flow ratio of N 2 gas / Ar gas = 20 / 5000 sccm. The experimental result shown in Fig. 10A is that a SiN film 102 having a thickness of about 18.6 nm can be formed on the base film 101. Further, in the experimental results shown in Fig. 10A, although the thickness of the base film 101 after the film formation treatment was reduced from about 62.4 nm to about 52.3 nm, the amount of reduction in film thickness was small. Further, in the present experiment, no void was observed inside the base film 101, and no void was observed between the base film 101 and the base substrate 100.

圖10B係顯示使用N2 氣體/Ar氣體=20/3000sccm之流量比的反應氣體進行成膜處理時基板剖面之一例的示意圖。圖10B所示之實驗結果係可在基底膜101上形成厚度大約17.4nm之SiN膜102。此外,圖10B所示之實驗結果中,雖然成膜處理後之基底膜101的厚度由大約62.4nm減少至大約54.3nm,但膜厚之減少量小。另外,在本實驗中,在基底膜101內部未發現空隙,且基底膜101與基底基板100之間亦未發現空隙。Fig. 10B is a schematic view showing an example of a cross section of a substrate when a film formation process is performed using a reaction gas having a flow ratio of N 2 gas / Ar gas = 20 / 3000 sccm. The experimental result shown in Fig. 10B is that a SiN film 102 having a thickness of about 17.4 nm can be formed on the base film 101. Further, in the experimental results shown in Fig. 10B, although the thickness of the base film 101 after the film formation treatment was reduced from about 62.4 nm to about 54.3 nm, the amount of reduction in film thickness was small. Further, in the present experiment, no void was observed inside the base film 101, and no void was observed between the base film 101 and the base substrate 100.

圖10C係顯示使用N2 氣體/Ar氣體=20/1000sccm之流量比的反應氣體進行成膜處理時基板剖面之一例的示意圖。圖10C所示之實驗結果係可在基底膜101上形成厚度大約20.1nm之SiN膜102。此外,圖10C所示之實驗結果中,雖然成膜處理後之基底膜101的厚度由大約62.4nm減少至大約55.4nm,但膜厚之減少量小。另外,在本實驗中,在基底膜101內部未發現空隙,且基底膜101與基底基板100之間亦未發現空隙。Fig. 10C is a schematic view showing an example of a cross section of a substrate when a film formation process is performed using a reaction gas having a flow ratio of N 2 gas / Ar gas = 20 / 1000 sccm. The experimental result shown in Fig. 10C is that a SiN film 102 having a thickness of about 20.1 nm can be formed on the base film 101. Further, in the experimental results shown in Fig. 10C, although the thickness of the base film 101 after the film formation treatment was reduced from about 62.4 nm to about 55.4 nm, the amount of reduction in film thickness was small. Further, in the present experiment, no void was observed inside the base film 101, and no void was observed between the base film 101 and the base substrate 100.

圖10D係顯示使用N2 氣體/Ar氣體=1000/0sccm之流量比的反應氣體進行成膜處理時基板剖面之一例的示意圖。此外,圖10D所示之實驗中,反應氣體不含Ar氣體。圖10D所示之實驗結果係可在基底膜101上形成厚度大約22.5nm之SiN膜102。但是,圖10D所示之實驗結果中,基底膜101之厚度由大約62.4nm減少至大約46.5nm,膜厚之減少量大。另外,如圖10D所示地,在基底膜101內部產生空隙,且基底膜101之一部份由基底基板100剝離。Fig. 10D is a schematic view showing an example of a cross section of a substrate when a film formation process is performed using a reaction gas having a flow ratio of N 2 gas / Ar gas = 1000 / 0 sccm. Further, in the experiment shown in Fig. 10D, the reaction gas contained no Ar gas. The experimental result shown in Fig. 10D is such that an SiN film 102 having a thickness of about 22.5 nm can be formed on the base film 101. However, in the experimental results shown in Fig. 10D, the thickness of the base film 101 was reduced from about 62.4 nm to about 46.5 nm, and the reduction in film thickness was large. Further, as shown in FIG. 10D, a void is generated inside the base film 101, and a part of the base film 101 is peeled off from the base substrate 100.

圖11係匯總圖10A至圖10D所示之實驗結果的表。如圖11所示地,反應氣體只使用N2 氣體進行成膜處理時,基底膜101之膜厚的減少量大。此外,在此情形中,如圖10D所示地,在基底膜101內產生空隙等之破壞。另一方面,反應氣體使用N2 氣體及Ar氣體之混合氣體時,基底膜101之膜厚的減少量比反應氣體只使用N2 氣體進行成膜處理時小得多。另外,在此情形中,如圖10A至圖10C所示地,基底膜101內亦未發現空隙等之破壞產生。Fig. 11 is a table summarizing the experimental results shown in Figs. 10A to 10D. As shown in FIG. 11, when the reaction gas is subjected to film formation treatment using only N 2 gas, the amount of reduction in the film thickness of the base film 101 is large. Further, in this case, as shown in FIG. 10D, breakage of voids or the like is generated in the base film 101. On the other hand, when a mixed gas of N 2 gas and Ar gas is used as the reaction gas, the amount of decrease in the thickness of the base film 101 is much smaller than when the reaction gas is formed by using only N 2 gas. Further, in this case, as shown in FIGS. 10A to 10C, no breakage of voids or the like was observed in the base film 101.

這是因為藉由在反應氣體中加入Ar氣體等之惰性氣體,電漿之密度上升,且SiN膜102之成膜速度增加,在對基底膜101之破壞變大前,SiN膜102之成膜終止。因此,為了減少基底膜101之膜厚減少量,並抑制在基底膜101內產生空隙等之破壞,反應氣體宜使用N2 氣體及Ar氣體之混合氣體。此外,由圖10A至圖10D所示之實驗結果來看,為了減少基底膜101之膜厚減少量,並抑制在基底膜101內產生空隙等之破壞,N2 氣體之流量與Ar氣體之流量的比宜為N2 氣體/Ar氣體20/1000sccm=1/50以下。This is because the density of the plasma is increased by the addition of an inert gas such as Ar gas to the reaction gas, and the film formation speed of the SiN film 102 is increased, and the film formation of the SiN film 102 is made before the destruction of the base film 101 becomes large. termination. Therefore, in order to reduce the amount of film thickness reduction of the base film 101 and to suppress the occurrence of voids or the like in the base film 101, a mixed gas of N 2 gas and Ar gas is preferably used as the reaction gas. Further, from the experimental results shown in Figs. 10A to 10D, in order to reduce the film thickness reduction amount of the base film 101 and suppress the occurrence of voids or the like in the base film 101, the flow rate of the N 2 gas and the flow rate of the Ar gas The ratio is preferably N 2 gas/Ar gas 20/1000 sccm = 1/50 or less.

此外,在理想之ALD中,成膜速度與基板旋轉速度相關,而與電漿密度無關。但是,實際上,Ar氣體之流量小時,由於氮自由基之存在機率降低,假設可氮化之位置為100時,只氮化大約60。結果,Ar氣體之流量小時,成膜速度變慢。若成膜速度變快,由於基底膜與氮自由基形成C-N鍵之機率亦減少,基底膜之破壞可減少。Furthermore, in an ideal ALD, the film formation rate is related to the substrate rotation speed regardless of the plasma density. However, in actuality, when the flow rate of the Ar gas is small, the probability of existence of the nitrogen radical is lowered, and when the position where the nitriding is performed is 100, only about 60 is nitrided. As a result, when the flow rate of the Ar gas is small, the film formation speed becomes slow. If the film formation speed is increased, the probability of forming a C-N bond between the base film and the nitrogen radical is also reduced, and the destruction of the base film can be reduced.

接著,進行改變供給微波之天線22a數目、及由天線22a供給之微波功率的實驗,並檢討可抑制減少基底膜101之膜厚或產生空隙等破壞之條件的範圍。圖12A至圖12E係顯示改變天線22a之數目及功率來進行成膜處理時基板W剖面之一例的示意圖。此外,在圖12A至圖12D所示之實驗中,與圖8A所示之基板W同樣地,使用形成有大約62.4nm之基底膜101的基板W。另外,使用DCS作為前驅物氣體。再者,在圖12A至圖12D所示之實驗中,電漿處理中之基板W的溫度係300℃,且使用供給微波之天線22a-2及22a-3,而N2 氣體之流量與Ar氣體之流量的比係N2 氣體/Ar氣體=20/1000sccm,且載置台14之旋轉速度係20rpm。Next, an experiment of changing the number of antennas 22a for supplying microwaves and the microwave power supplied from the antenna 22a is performed, and a range in which the conditions for reducing the film thickness of the base film 101 or the occurrence of voids or the like is suppressed can be examined. 12A to 12E are schematic views showing an example of a cross section of the substrate W when the number and power of the antennas 22a are changed to perform a film formation process. Further, in the experiment shown in FIGS. 12A to 12D, a substrate W on which the base film 101 of about 62.4 nm was formed was used in the same manner as the substrate W shown in FIG. 8A. In addition, DCS was used as the precursor gas. Further, in the experiments shown in FIGS. 12A to 12D, the temperature of the substrate W in the plasma treatment was 300 ° C, and the antennas 22a-2 and 22a-3 for supplying microwaves were used, and the flow rate of the N 2 gas and Ar were used. The ratio of the flow rate of the gas was N 2 gas / Ar gas = 20 / 1000 sccm, and the rotation speed of the mounting table 14 was 20 rpm.

圖12A係顯示使用1個天線22a(天線22a-3),且設由天線供給之微波功率為0.5kW來進行成膜處理時基板W剖面之一例的示意圖。此外,在圖12A所示之實驗中,未使用天線22a-1及22a-2。圖12所示之實驗結果係可在基底膜101上形成厚度大約16.6nm之SiN膜102。FIG. 12A is a schematic diagram showing an example of a cross section of a substrate W when a single film 22a (antenna 22a-3) is used and a microwave power supplied from an antenna is 0.5 kW to perform a film formation process. Further, in the experiment shown in Fig. 12A, the antennas 22a-1 and 22a-2 were not used. The experimental result shown in Fig. 12 is that a SiN film 102 having a thickness of about 16.6 nm can be formed on the base film 101.

但是,圖12A所示之實驗結果係在成膜處理後之基底膜101內部產生空隙,且在其影響下,基底膜101之厚度由大約62.4nm膨脹至大約67.0nm。此外,基底膜101與基底基板100之間亦發現空隙,可考慮基底膜101與基底基板100之密接力降低。However, the experimental results shown in Fig. 12A generate voids inside the base film 101 after the film formation treatment, and under the influence thereof, the thickness of the base film 101 is expanded from about 62.4 nm to about 67.0 nm. Further, a void is also found between the base film 101 and the base substrate 100, and the adhesion between the base film 101 and the base substrate 100 can be considered to be lowered.

圖12B係顯示使用2個天線22a(天線22a-2及22a-3),且設由各天線22a供給之微波功率為1.0kW來進行成膜處理時基板W剖面之一例的剖面圖。在本實驗中,由天線22a供給之微波功率的總和為2.0kW。此外,在圖12B所示之實驗中,未使用天線22a-1。FIG. 12B is a cross-sectional view showing an example of a cross section of the substrate W when the film formation process is performed using the two antennas 22a (the antennas 22a-2 and 22a-3) and the microwave power supplied from each antenna 22a is 1.0 kW. In this experiment, the sum of the microwave powers supplied from the antenna 22a was 2.0 kW. Further, in the experiment shown in Fig. 12B, the antenna 22a-1 was not used.

圖12B所示之實驗結果係可在基底膜101上形成厚度大約17.4nm之SiN膜102。此外,圖12B所示之實驗結果中,雖然成膜處理後之基底膜101之厚度由大約62.4nm減少至大約55.0nm,但膜厚之減少量小。另外,在本實驗中,在基底膜101內部未發現空隙,且基底膜101與基底基板100之間亦未發現空隙。The experimental result shown in Fig. 12B is that a SiN film 102 having a thickness of about 17.4 nm can be formed on the base film 101. Further, in the experimental results shown in Fig. 12B, although the thickness of the base film 101 after the film formation treatment was reduced from about 62.4 nm to about 55.0 nm, the amount of reduction in film thickness was small. Further, in the present experiment, no void was observed inside the base film 101, and no void was observed between the base film 101 and the base substrate 100.

圖12C係顯示使用1個天線22a(天線22a-3),且設由天線供給之微波功率為2.0kW來進行成膜處理時基板W剖面之一例的剖面圖。此外,在圖12C所示之實驗中,未使用天線22a-1及22a-2。12C is a cross-sectional view showing an example of a cross section of the substrate W when a single film 22a (antenna 22a-3) is used and a microwave power supplied from the antenna is 2.0 kW to perform a film formation process. Further, in the experiment shown in Fig. 12C, the antennas 22a-1 and 22a-2 were not used.

圖12C所示之實驗結果係可在基底膜101上形成厚度大約13.4nm之SiN膜102。此外,圖12C所示之實驗結果中,雖然成膜處理後之基底膜101之厚度由大約62.4nm減少至大約52.5nm,但膜厚之減少量小。另外,在本實驗中,在基底膜101內部未發現空隙,且基底膜101與基底基板100之間亦未發現空隙。The experimental result shown in Fig. 12C is that a SiN film 102 having a thickness of about 13.4 nm can be formed on the base film 101. Further, in the experimental results shown in Fig. 12C, although the thickness of the base film 101 after the film formation treatment was reduced from about 62.4 nm to about 52.5 nm, the amount of reduction in film thickness was small. Further, in the present experiment, no void was observed inside the base film 101, and no void was observed between the base film 101 and the base substrate 100.

圖12D係顯示使用2個天線22a(天線22a-2及22a-3),且設由各天線22a供給之微波功率為2.0kW來進行成膜處理時基板W剖面之一例的剖面圖。在本實驗中,由天線22a供給之微波功率的總和為4.0kW。此外,在圖12D所示之實驗中,未使用天線22a-1。FIG. 12D is a cross-sectional view showing an example of a cross section of the substrate W when the film formation process is performed using the two antennas 22a (the antennas 22a-2 and 22a-3) and the microwave power supplied from each antenna 22a is 2.0 kW. In this experiment, the sum of the microwave powers supplied from the antenna 22a was 4.0 kW. Further, in the experiment shown in Fig. 12D, the antenna 22a-1 was not used.

圖12D所示之實驗結果係可在基底膜101上形成厚度大約18.2nm之SiN膜102。此外,圖12D所示之實驗結果中,雖然成膜處理後之基底膜101之厚度由大約62.4nm減少至大約60.1nm,但膜厚之減少量小。另外,在本實驗中,在基底膜101內部未發現空隙,且基底膜101與基底基板100之間亦未發現空隙。The experimental result shown in Fig. 12D is such that a SiN film 102 having a thickness of about 18.2 nm can be formed on the base film 101. Further, in the experimental results shown in Fig. 12D, although the thickness of the base film 101 after the film formation treatment was reduced from about 62.4 nm to about 60.1 nm, the amount of reduction in film thickness was small. Further, in the present experiment, no void was observed inside the base film 101, and no void was observed between the base film 101 and the base substrate 100.

圖12E係顯示使用2個天線22a(天線22a-2及22a-3),且設由各天線22a供給之微波功率為4.0kW來進行成膜處理時基板W剖面之一例的剖面圖。在本實驗中,由天線22a供給之微波功率的總和為8.0kW。此外,在圖12E所示之實驗中,未使用天線22a-1。FIG. 12E is a cross-sectional view showing an example of a cross section of the substrate W when the film formation process is performed using the two antennas 22a (the antennas 22a-2 and 22a-3) and the microwave power supplied from each antenna 22a is 4.0 kW. In this experiment, the sum of the microwave powers supplied from the antenna 22a was 8.0 kW. Further, in the experiment shown in Fig. 12E, the antenna 22a-1 was not used.

圖12E所示之實驗結果係可在基底膜101上形成厚度大約20.1nm之SiN膜102。此外,圖12E所示之實驗結果係雖然成膜處理後之基底膜101之厚度由大約62.4nm減少至大約55.4nm,但膜厚之減少量小。另外,在本實驗中,在基底膜101內部未發現空隙,且基底膜101與基底基板100之間亦未發現空隙。The experimental result shown in Fig. 12E is that a SiN film 102 having a thickness of about 20.1 nm can be formed on the base film 101. Further, the experimental results shown in Fig. 12E are such that although the thickness of the base film 101 after the film formation treatment is reduced from about 62.4 nm to about 55.4 nm, the reduction in film thickness is small. Further, in the present experiment, no void was observed inside the base film 101, and no void was observed between the base film 101 and the base substrate 100.

圖13係匯總圖12A至圖12E所示之實驗結果的表。如圖13所示地,由天線22a供給之微波功率的總和為0.5kW時,基底膜101產生變質,並產生在基底膜101內產生空隙等之破壞。另一方面,由天線22a供給之微波功率的總和為2.0kW以上時,未發現基底膜101變質或產生空隙等之破壞。Fig. 13 is a table summarizing the experimental results shown in Figs. 12A to 12E. As shown in FIG. 13, when the sum of the microwave powers supplied from the antenna 22a is 0.5 kW, the base film 101 is deteriorated, and breakage or the like is generated in the base film 101. On the other hand, when the sum of the microwave powers supplied from the antenna 22a is 2.0 kW or more, the base film 101 is not deteriorated or the voids or the like are not damaged.

若供給之微波功率低,N2 氣體分子在電漿中未充分解離,且電漿所包含之氮原子的離子或自由基數變少。因此,成膜速度慢,且在到形成預定厚度之SiN膜102為止的期間,包含基底膜101之基板W長時間暴露在高溫環境下。因此,基底膜101會受到熱的影響而變質。If the microwave power supplied is low, the N 2 gas molecules are not sufficiently dissociated in the plasma, and the number of ions or radicals of the nitrogen atoms contained in the plasma is small. Therefore, the film formation speed is slow, and the substrate W including the base film 101 is exposed to a high temperature environment for a long period of time until the SiN film 102 having a predetermined thickness is formed. Therefore, the base film 101 is deteriorated by the influence of heat.

相對於此,由天線22a供給之微波功率的總和為例如2.0kW以上時,在電漿中解離之N2 氣體分子增加,且電漿所包含之氮原子的離子或自由基數增加。因此,成膜速度快,且到形成預定厚度之SiN膜102為止的時間短。因此,包含基底膜101之基板W暴露在高溫環境下的時間短,且基底膜101受熱之影響減少,可抑制基底膜101之變質。On the other hand, when the sum of the microwave powers supplied from the antenna 22a is, for example, 2.0 kW or more, the N 2 gas molecules dissociated in the plasma increase, and the number of ions or radicals of the nitrogen atoms contained in the plasma increases. Therefore, the film formation speed is fast, and the time until the SiN film 102 of a predetermined thickness is formed is short. Therefore, the substrate W including the base film 101 is exposed to a high temperature environment for a short period of time, and the base film 101 is less affected by heat, and the deterioration of the base film 101 can be suppressed.

因此,為抑制基底膜101之變質,並在基底膜101上形成預定厚度之SiN膜102,由天線22a供給之微波功率的總和宜為例如2.0kW以上。Therefore, in order to suppress the deterioration of the base film 101 and form the SiN film 102 of a predetermined thickness on the base film 101, the sum of the microwave powers supplied from the antenna 22a is preferably, for example, 2.0 kW or more.

接著,進行實驗,該實驗係藉由N2 氣體及Ar氣體之混合氣體的電漿,在基底膜101上形成預定厚度之SiN膜(第1氮化膜),並以此為保護膜,在其上藉由NH3 氣體及H2 氣體之混合氣體的電漿形成SiN膜(第2氮化膜)。圖14係顯示形成保護膜後形成SiN膜之成膜處理之一例的流程圖。Next, an experiment was conducted in which a SiN film (first nitride film) having a predetermined thickness was formed on the base film 101 by a plasma of a mixed gas of N 2 gas and Ar gas, and this was used as a protective film. An SiN film (second nitride film) is formed by a plasma of a mixed gas of NH 3 gas and H 2 gas. Fig. 14 is a flow chart showing an example of a film forming process for forming a SiN film after forming a protective film.

首先,將基底基板100上形成有基底膜101之基板W搬入成膜裝置10之處理容器12內(S100)。然後,實行保護膜形成步驟(S101)。在保護膜形成步驟中,由第1氣體供給部16,噴射作為前驅物氣體之DCS在藉載置台14之旋轉而移動的基板W上。接著,藉由排氣部18及第2氣體供給部20之作用由基板W去除過剩地吸附在基板W之表面上的前驅物氣體。然後,將藉載置台14之旋轉而移動的基板W暴露在由反應氣體供給部22c供給作為反應氣體之N2 氣體及Ar氣體之混合氣體的電漿中。藉此,在基底膜101上形成保護膜。First, the substrate W on which the base film 101 is formed on the base substrate 100 is carried into the processing container 12 of the film forming apparatus 10 (S100). Then, a protective film forming step (S101) is carried out. In the protective film forming step, the DCS as the precursor gas is ejected onto the substrate W that is moved by the rotation of the loading table 14 by the first gas supply unit 16. Then, the precursor gas that is excessively adsorbed on the surface of the substrate W is removed from the substrate W by the action of the exhaust portion 18 and the second gas supply portion 20. Then, the substrate W that has been moved by the rotation of the stage 14 is exposed to a plasma in which a mixed gas of N 2 gas and Ar gas as a reaction gas is supplied from the reaction gas supply unit 22c. Thereby, a protective film is formed on the base film 101.

此外,在保護膜形成步驟中,N2 氣體之流量及Ar氣體之流量的比係N2 氣體/Ar氣體=20/1000sccm,使用2個天線22a(天線22a-2及22a-3),且由各天線22a供給之微波功率為2.0kW。此外,電漿處理中之基板W的溫度係300℃,且載置台14之旋轉速度係20rpm。Further, in the protective film forming step, the ratio of the flow rate of the N 2 gas to the flow rate of the Ar gas is N 2 gas / Ar gas = 20 / 1000 sccm, and two antennas 22a (antennas 22a-2 and 22a-3) are used, and The microwave power supplied from each antenna 22a was 2.0 kW. Further, the temperature of the substrate W in the plasma treatment was 300 ° C, and the rotation speed of the mounting table 14 was 20 rpm.

然後,到在基底膜101上形成預定厚度之保護膜為止(S102:否(No)),重複預定次步驟S101所示之保護膜形成步驟。在本實驗中,到形成例如厚度大約3nm之保護膜為止,重複步驟S101所示之保護膜形成步驟。重複預定次保護膜形成步驟後(S102:是(Yes)),實行氮化膜形成步驟(S103)。Then, until a protective film having a predetermined thickness is formed on the base film 101 (S102: No), the protective film forming step shown in the step S101 is repeated a predetermined time. In the present experiment, the protective film forming step shown in step S101 was repeated until a protective film having a thickness of, for example, about 3 nm was formed. After the predetermined protective film forming step is repeated (S102: Yes), a nitride film forming step (S103) is performed.

在氮化膜形成步驟中,由第1氣體供給部16,噴射作為前驅物氣體之DCS在藉載置台14之旋轉而移動的基板W上。接著,藉由排氣部18及第2氣體供給部20之作用由基板W去除過剩地吸附在基板W之表面上的前驅物氣體。然後,將藉載置台14之旋轉而移動的基板W暴露在由反應氣體供給部22c供給作為反應氣體之NH3 氣體及H2 氣體之混合氣體的電漿中。藉此,在保護膜上形成SiN膜。In the nitride film forming step, the DCS as the precursor gas is ejected onto the substrate W that is moved by the rotation of the mounting table 14 by the first gas supply unit 16. Then, the precursor gas that is excessively adsorbed on the surface of the substrate W is removed from the substrate W by the action of the exhaust portion 18 and the second gas supply portion 20. Then, the substrate W that has been moved by the rotation of the stage 14 is exposed to a plasma in which a mixed gas of NH 3 gas and H 2 gas as a reaction gas is supplied from the reaction gas supply unit 22c. Thereby, a SiN film is formed on the protective film.

此外,在氮化膜形成步驟中,NH3 氣體之流量及H2 氣體之流量的比係NH3 氣體/H2 氣體=750/4000sccm,使用2個天線22a(天線22a-2及22a-3),且由各天線22a供給之微波功率為4.0kW。此外,電漿處理中之基板W的溫度係300℃,且載置台14之旋轉速度係20rpm。Further, in the nitride film forming step, the ratio of the flow rate of the NH 3 gas to the flow rate of the H 2 gas is NH 3 gas / H 2 gas = 750 / 4000 sccm, and two antennas 22a are used (antennas 22a-2 and 22a-3) The microwave power supplied from each antenna 22a is 4.0 kW. Further, the temperature of the substrate W in the plasma treatment was 300 ° C, and the rotation speed of the mounting table 14 was 20 rpm.

然後,到在保護膜上形成預定厚度之SiN膜為止(S104:No),重複預定次步驟S103所示之氮化膜形成步驟。在本實驗中,到形成例如厚度大約17nm之SiN膜為止,重複步驟S103所示之氮化膜形成步驟。重複預定次氮化膜形成步驟後(S104:Yes),由處理容器12搬出基板W(S105),本流程圖所示之成膜處理結束。Then, until a SiN film having a predetermined thickness is formed on the protective film (S104: No), the predetermined step of forming a nitride film shown in step S103 is repeated. In the present experiment, the step of forming a nitride film shown in step S103 was repeated until a SiN film having a thickness of, for example, about 17 nm was formed. After the predetermined step of forming the nitride film is repeated (S104: Yes), the substrate W is carried out by the processing container 12 (S105), and the film forming process shown in this flowchart is completed.

圖15係顯示藉由圖14所示之成膜處理成膜之基板剖面的一例的示意圖。在圖15所示之基板W中,在基底膜101上形成膜厚大約22.5nm之SiN膜102。圖15所示之SiN膜102包含由N2 氣體及Ar氣體之混合氣體之電漿形成的保護膜、及由NH3 氣體及H2 氣體之混合氣體之電漿形成的SiN膜。Fig. 15 is a schematic view showing an example of a cross section of a substrate formed by film formation processing shown in Fig. 14. In the substrate W shown in FIG. 15, an SiN film 102 having a film thickness of about 22.5 nm is formed on the base film 101. The SiN film 102 shown in FIG. 15 includes a protective film formed of a plasma of a mixed gas of N 2 gas and Ar gas, and an SiN film formed of a plasma of a mixed gas of NH 3 gas and H 2 gas.

在本實驗中,使用形成有膜厚大約60nm之基底膜101的基板W。如圖15所示地,成膜處理後之基底膜101的厚度係大約59.3nm,且相對成膜前之基底膜101幾乎沒有變化。此外,在本實驗中,在基底膜101內部未發現空隙,且基底膜101與基底基板100之間亦未發現空隙。另外,亦未發現基底膜101之變質。In this experiment, a substrate W formed with a base film 101 having a film thickness of about 60 nm was used. As shown in Fig. 15, the thickness of the base film 101 after the film formation treatment was about 59.3 nm, and there was almost no change with respect to the base film 101 before film formation. Further, in the present experiment, no void was observed inside the base film 101, and no void was observed between the base film 101 and the base substrate 100. In addition, deterioration of the base film 101 was not observed.

接著,重複實驗,結果了解由N2 氣體及Ar氣體之混合氣體之電漿形成的保護膜厚度即使薄到0.5至1.0nm,亦具有作為基底膜101之保護膜的機能,可抑制基底膜101產生空隙。本實驗之目的係在含有碳之基底膜101上,藉由NH3 氣體及H2 氣體之混合氣體之電漿形成SiN膜。由N2 氣體及Ar氣體之混合氣體之電漿形成的保護膜係具有與由NH3 氣體及H2 氣體之混合氣體之電漿形成的SiN膜不同性質的膜。因此,保護膜以極薄為佳。因此,保護膜之厚度宜為0.5至1.0nm之厚度。Then, the experiment was repeated, and it was found that the thickness of the protective film formed of the plasma of the mixed gas of the N 2 gas and the Ar gas was as small as 0.5 to 1.0 nm, and the function as the protective film of the base film 101 was suppressed, and the base film 101 was suppressed. Create a gap. The purpose of this experiment is to form a SiN film on a base film 101 containing carbon by a plasma of a mixed gas of NH 3 gas and H 2 gas. A protective film formed of a plasma of a mixed gas of N 2 gas and Ar gas has a film having a property different from that of a SiN film formed of a plasma of a mixed gas of NH 3 gas and H 2 gas. Therefore, the protective film is preferably extremely thin. Therefore, the thickness of the protective film is preferably from 0.5 to 1.0 nm.

以上,說明了一實施形態。依據本實施形態之成膜裝置10,可抑制含有碳原子之基底膜膜厚的減少,且可在基底膜上形成預定厚度之氮化膜。One embodiment has been described above. According to the film forming apparatus 10 of the present embodiment, it is possible to suppress a decrease in the thickness of the underlying film containing carbon atoms, and to form a nitride film having a predetermined thickness on the underlying film.

此外,本發明不限於上述實施形態,在其要旨之範圍內可有許多變形。Further, the present invention is not limited to the above embodiments, and many modifications are possible within the scope of the gist of the invention.

例如,在上述實施形態中,雖然形成於保護膜上之SiN膜藉由NH3 氣體及H2 氣體之混合氣體之電漿形成,但揭示之技術不限於此。例如,形成於保護膜上之SiN膜亦可藉由N2 氣體及H2 氣體之混合氣體之電漿形成。若不設保護膜,而在基底膜上藉由N2 氣體及H2 氣體之混合氣體之電漿形成SiN膜,則含有碳原子之基底膜膜厚的減少量大,但在形成於基底膜上之保護膜上,藉由N2 氣體及H2 氣體之混合氣體之電漿形成SiN膜,可抑制基底膜之膜厚的減少,且可在基底膜上形成預定厚度之氮化膜。For example, in the above embodiment, the SiN film formed on the protective film is formed of a plasma of a mixed gas of NH 3 gas and H 2 gas, but the disclosed technology is not limited thereto. For example, the SiN film formed on the protective film may be formed by a plasma of a mixed gas of N 2 gas and H 2 gas. If a SiN film is formed on a base film by a plasma of a mixed gas of N 2 gas and H 2 gas without a protective film, the thickness of the base film containing carbon atoms is greatly reduced, but it is formed on the base film. On the upper protective film, a SiN film is formed by a plasma of a mixed gas of N 2 gas and H 2 gas, whereby a decrease in film thickness of the base film can be suppressed, and a nitride film having a predetermined thickness can be formed on the base film.

此外,在上述實施形態中,雖然舉例說明了使用微波之半批式成膜裝置10,但成膜裝置10不限於此。例如,成膜裝置10可為使用微波之ALD方式的成膜裝置,可為單片式或批式之成膜裝置,亦可為使用高頻之CVD(化學蒸氣沈積;Chemical Vapor Deposition)方式的成膜裝置。Further, in the above-described embodiment, the half-batch film forming apparatus 10 using microwaves has been exemplified, but the film forming apparatus 10 is not limited thereto. For example, the film forming apparatus 10 may be a film forming apparatus using an ALD method using microwaves, and may be a monolithic or batch film forming apparatus, or may be a high frequency CVD (Chemical Vapor Deposition) method. Film forming device.

由上述內容可了解本發明之各種實施例係為了達成說明之目的而記載,且,可不脫離本發明之範圍及思想地進行各種變形。因此,在此揭示之各種實施例不是為了限制由以下各請求項所指定之本質的範圍及思想。It is to be understood that the various embodiments of the present invention are described in the foregoing, Therefore, the various embodiments disclosed herein are not intended to limit the scope and spirit of the nature of the invention.

10‧‧‧成膜裝置
12‧‧‧處理容器
12a‧‧‧下部構件
12b‧‧‧上部構件
12q‧‧‧排氣路
12r‧‧‧氣體供給路
14‧‧‧載置台
14a‧‧‧基板載置區域
16‧‧‧第1氣體供給部
16a‧‧‧噴射部
16g‧‧‧氣體供給源
16h‧‧‧噴射口
18‧‧‧排氣部
18a‧‧‧排氣口
18d‧‧‧空間
18g‧‧‧間隙
18q‧‧‧排氣路
20‧‧‧第2氣體供給部
20a‧‧‧噴射口
20c‧‧‧流量控制器
20d‧‧‧空間
20g‧‧‧氣體供給源
20p‧‧‧間隙
20r‧‧‧氣體供給路
20v‧‧‧閥
22‧‧‧電漿產生部
22a‧‧‧天線
22a-1‧‧‧天線
22a-2‧‧‧天線
22a-3‧‧‧天線
22b‧‧‧同軸波導管
22c‧‧‧反應氣體供給部
22h‧‧‧排氣部
24‧‧‧驅動機構
24a‧‧‧驅動裝置
24b‧‧‧旋轉軸
26‧‧‧加熱器
34‧‧‧排氣裝置
40‧‧‧頂板
42‧‧‧開槽板
44‧‧‧慢波板
46‧‧‧冷卻板
50b‧‧‧內側噴射口
50c‧‧‧流量控制部
50g‧‧‧氣體供給源
50v‧‧‧閥
51b‧‧‧外側噴射口
51c‧‧‧流量控制部
51v‧‧‧閥
52‧‧‧排氣裝置
60‧‧‧波導管
62a‧‧‧內側導體
62b‧‧‧外側導體
68‧‧‧微波產生器
70‧‧‧控制部
100‧‧‧基底基板
101‧‧‧基底膜
102‧‧‧SiN膜
103‧‧‧導體膜
121p‧‧‧氣體供給路
122p‧‧‧氣體供給路
123p‧‧‧氣體供給路
161‧‧‧內側氣體供給部
161a‧‧‧內側噴射部
161b‧‧‧彈性構件
161c‧‧‧流量控制器
161d‧‧‧緩衝空間
161p‧‧‧氣體供給路
161v‧‧‧閥
162‧‧‧中間氣體供給部
162a‧‧‧中間噴射部
162b‧‧‧彈性構件
162c‧‧‧流量控制器
162d‧‧‧緩衝空間
162p‧‧‧氣體供給路
162v‧‧‧閥
163‧‧‧外側氣體供給部
163a‧‧‧外側噴射部
163b‧‧‧彈性構件
163c‧‧‧流量控制器
163d‧‧‧緩衝空間
163p‧‧‧氣體供給路
163v‧‧‧閥
220‧‧‧分隔件
220h‧‧‧排氣區域
221‧‧‧蓋部
222‧‧‧溝部
A1‧‧‧內側環狀區域
A2‧‧‧中間環狀區域
A3‧‧‧外側環狀區域
AP‧‧‧開口
C‧‧‧處理室
G‧‧‧閘閥
L‧‧‧長度
DL‧‧‧預定距離
M1‧‧‧第1構件
M2‧‧‧第2構件
M3‧‧‧第3構件
M4‧‧‧第4構件
R1‧‧‧第1區域
R2‧‧‧第2區域
r1‧‧‧距離
r2‧‧‧距離
r3‧‧‧距離
r4‧‧‧距離
S100‧‧‧步驟
S101‧‧‧步驟
S102‧‧‧步驟
S103‧‧‧步驟
S104‧‧‧步驟
S105‧‧‧步驟
U‧‧‧單元
W‧‧‧基板
W1‧‧‧直徑
X‧‧‧軸線
10‧‧‧ film forming device
12‧‧‧Processing container
12a‧‧‧lower components
12b‧‧‧ upper member
12q‧‧‧ exhaust road
12r‧‧‧ gas supply road
14‧‧‧ mounting table
14a‧‧‧Substrate placement area
16‧‧‧1st gas supply department
16a‧‧‧Injection Department
16g‧‧‧ gas supply source
16h‧‧‧jet
18‧‧‧Exhaust Department
18a‧‧‧Exhaust port
18d‧‧‧ space
18g‧‧‧ gap
18q‧‧‧Exhaust road
20‧‧‧2nd gas supply department
20a‧‧‧jet
20c‧‧‧Flow Controller
20d‧‧‧ space
20g‧‧‧ gas supply source
20p‧‧‧ gap
20r‧‧‧ gas supply road
20v‧‧‧ valve
22‧‧‧ Plasma Production Department
22a‧‧‧Antenna
22a-1‧‧‧Antenna
22a-2‧‧‧Antenna
22a-3‧‧‧Antenna
22b‧‧‧ coaxial waveguide
22c‧‧‧Reactive Gas Supply Department
22h‧‧‧Exhaust Department
24‧‧‧ drive mechanism
24a‧‧‧ drive
24b‧‧‧Rotary axis
26‧‧‧heater
34‧‧‧Exhaust device
40‧‧‧ top board
42‧‧‧ slotted board
44‧‧‧ Slow wave board
46‧‧‧Cooling plate
50b‧‧‧Inside injection port
50c‧‧‧Flow Control Department
50g‧‧‧ gas supply source
50v‧‧‧ valve
51b‧‧‧Outer jet
51c‧‧‧Flow Control Department
51v‧‧‧ valve
52‧‧‧Exhaust device
60‧‧‧waveguide
62a‧‧‧Inside conductor
62b‧‧‧Outer conductor
68‧‧‧Microwave generator
70‧‧‧Control Department
100‧‧‧Base substrate
101‧‧‧ basement membrane
102‧‧‧SiN film
103‧‧‧Conductor film
121p‧‧‧ gas supply road
122p‧‧‧ gas supply road
123p‧‧‧ gas supply road
161‧‧‧Internal Gas Supply Department
161a‧‧‧Inside Jetting Department
161b‧‧‧Flexible components
161c‧‧‧Flow Controller
161d‧‧‧ buffer space
161p‧‧‧ gas supply road
161v‧‧‧ valve
162‧‧‧Intermediate Gas Supply Department
162a‧‧‧Intermediate Jet Department
162b‧‧‧Flexible components
162c‧‧‧Flow Controller
162d‧‧‧ buffer space
162p‧‧‧ gas supply road
162v‧‧‧ valve
163‧‧‧Outside Gas Supply Department
163a‧‧‧Outer Jet Department
163b‧‧‧Flexible components
163c‧‧‧Flow Controller
163d‧‧‧ buffer space
163p‧‧‧ gas supply road
163v‧‧‧ valve
220‧‧‧Parts
220h‧‧‧Exhaust area
221‧‧‧ 盖部
222‧‧‧Ditch
A1‧‧‧inside annular zone
A2‧‧‧ intermediate ring zone
A3‧‧‧Outer annular area
AP‧‧‧ openings
C‧‧‧Processing room
G‧‧‧ gate valve
L‧‧‧ length
DL‧‧‧Predetermined distance
M1‧‧‧1st component
M2‧‧‧ second component
M3‧‧‧3rd component
M4‧‧‧4th building
R1‧‧‧1st area
R2‧‧‧2nd area
R1‧‧‧ distance
R2‧‧‧ distance
R3‧‧‧ distance
R4‧‧‧ distance
S100‧‧‧ steps
S101‧‧‧Steps
S102‧‧‧Steps
S103‧‧‧Steps
S104‧‧‧Steps
S105‧‧‧Steps
Unit U‧‧‧
W‧‧‧Substrate
W1‧‧‧ diameter
X‧‧‧ axis

圖1係顯示成膜裝置之一例的剖面圖。Fig. 1 is a cross-sectional view showing an example of a film forming apparatus.

圖2係顯示由上方看時之成膜裝置之一例的示意圖。Fig. 2 is a schematic view showing an example of a film forming apparatus when viewed from above.

圖3係顯示圖1中軸線X左側部分之一例的放大剖面圖。Fig. 3 is an enlarged cross-sectional view showing an example of a left portion of the axis X in Fig. 1.

圖4係顯示圖1中軸線X左側部分之一例的放大剖面圖。Fig. 4 is an enlarged cross-sectional view showing an example of a left portion of the axis X in Fig. 1.

圖5係顯示單元U下面之一例的圖。Fig. 5 is a view showing an example of the lower portion of the unit U.

圖6係顯示圖1中軸線X右側部分之一例的放大剖面圖。Fig. 6 is an enlarged cross-sectional view showing an example of a right portion of the axis X in Fig. 1.

圖7A係顯示進行成膜處理前之基板剖面之一例的示意圖。Fig. 7A is a schematic view showing an example of a cross section of a substrate before performing a film formation process.

圖7B係顯示使用NH3 氣體及H2 氣體之混合氣體進行成膜處理時基板剖面之一例的示意圖。Fig. 7B is a schematic view showing an example of a cross section of a substrate when a film forming process is performed using a mixed gas of NH 3 gas and H 2 gas.

圖8A係顯示進行成膜處理前之基板剖面之一例的示意圖。Fig. 8A is a schematic view showing an example of a cross section of a substrate before performing a film formation process.

圖8B係顯示使用NH3 氣體進行成膜處理時基板剖面之一例的示意圖。Fig. 8B is a schematic view showing an example of a cross section of a substrate when a film formation process is performed using NH 3 gas.

圖9係顯示使用N2 氣體及Ar氣體之混合氣體進行成膜處理時基板剖面之一例的示意圖。FIG. 9 is a schematic view showing an example of a cross section of a substrate when a film formation process is performed using a mixed gas of N 2 gas and Ar gas.

圖10A係顯示使用N2 氣體/Ar氣體=20/5000sccm之流量比的反應氣體進行成膜處理時基板剖面之一例的示意圖。Fig. 10A is a schematic view showing an example of a cross section of a substrate when a film formation process is performed using a reaction gas having a flow ratio of N 2 gas / Ar gas = 20 / 5000 sccm.

圖10B係顯示使用N2 氣體/Ar氣體=20/3000sccm之流量比的反應氣體進行成膜處理時基板剖面之一例的示意圖。Fig. 10B is a schematic view showing an example of a cross section of a substrate when a film formation process is performed using a reaction gas having a flow ratio of N 2 gas / Ar gas = 20 / 3000 sccm.

圖10C係顯示使用N2 氣體/Ar氣體=20/1000sccm之流量比的反應氣體進行成膜處理時基板剖面之一例的示意圖。Fig. 10C is a schematic view showing an example of a cross section of a substrate when a film formation process is performed using a reaction gas having a flow ratio of N 2 gas / Ar gas = 20 / 1000 sccm.

圖10D係顯示使用N2 氣體/Ar氣體=1000/0sccm之流量比的反應氣體進行成膜處理時基板剖面之一例的示意圖。Fig. 10D is a schematic view showing an example of a cross section of a substrate when a film formation process is performed using a reaction gas having a flow ratio of N 2 gas / Ar gas = 1000 / 0 sccm.

圖11係匯總圖10A至圖10D所示之實驗結果的表。Fig. 11 is a table summarizing the experimental results shown in Figs. 10A to 10D.

圖12A係顯示使用1個天線,設由天線供給之微波功率為0.5kW來進行成膜處理時基板剖面之一例的示意圖。Fig. 12A is a schematic view showing an example of a cross section of a substrate when a film forming process is performed using a single antenna and a microwave power supplied from an antenna of 0.5 kW.

圖12B係顯示使用2個天線,設由各天線供給之微波功率為1.0kW來進行成膜處理時基板之一例的剖面圖。12B is a cross-sectional view showing an example of a substrate when a film forming process is performed using two antennas and a microwave power supplied from each antenna is 1.0 kW.

圖12C係顯示使用1個天線,設由天線供給之微波功率為2.0kW來進行成膜處理時基板剖面之一例的示意圖。Fig. 12C is a schematic view showing an example of a substrate cross-section when a film forming process is performed using a single antenna and a microwave power supplied from an antenna of 2.0 kW.

圖12D係顯示使用2個天線,設由各天線供給之微波功率為2.0kW來進行成膜處理時基板剖面之一例的示意圖。12D is a schematic view showing an example of a substrate cross-section when a film formation process is performed using two antennas and microwave power supplied from each antenna is 2.0 kW.

圖12E係顯示使用2個天線,設由各天線供給之微波功率為4.0kW來進行成膜處理時基板剖面之一例的示意圖。Fig. 12E is a schematic view showing an example of a substrate cross-section when a film formation process is performed using two antennas and microwave power supplied from each antenna is 4.0 kW.

圖13係匯總圖12A至圖12E所示之實驗結果的表。Fig. 13 is a table summarizing the experimental results shown in Figs. 12A to 12E.

圖14係顯示形成保護膜後形成SiN膜之成膜處理之一例的流程圖。Fig. 14 is a flow chart showing an example of a film forming process for forming a SiN film after forming a protective film.

圖15係顯示藉由N2 氣體及Ar氣體之混合氣體形成保護膜後形成SiN膜時基板剖面之一例的示意圖。Fig. 15 is a schematic view showing an example of a cross section of a substrate when a SiN film is formed by forming a protective film of a mixed gas of N 2 gas and Ar gas.

S100~S105‧‧‧步驟 S100~S105‧‧‧Steps

Claims (7)

一種成膜方法,在載置於成膜裝置之處理容器內並具有含有碳原子之含碳膜的被處理基板上,形成氮化膜,該成膜方法包含第1氮化膜形成步驟,而該第1氮化膜形成步驟係藉由包含不具有氫原子之氮化物氣體及惰性氣體的第1反應氣體之電漿,在該含碳膜上形成第1氮化膜,其中該第1反應氣體係N2氣體與Ar氣體之混合氣體,且其中N2氣體之流量對Ar氣體之流量的比率係1/50以下。 A film forming method for forming a nitride film on a substrate to be processed which is placed in a processing container of a film forming apparatus and having a carbon-containing film containing carbon atoms, the film forming method including a first nitride film forming step, and In the first nitride film forming step, a first nitride film is formed on the carbon-containing film by a plasma containing a first reaction gas containing a nitride gas of no hydrogen atom and an inert gas, wherein the first reaction A gas mixture of N 2 gas and Ar gas, and wherein the ratio of the flow rate of the N 2 gas to the flow rate of the Ar gas is 1/50 or less. 如申請專利範圍第1項之成膜方法,其中,在該第1氮化膜形成步驟中,該第1氮化膜係藉由原子層沉積(ALD;Atomic Layer Deposition)法形成。 The film forming method according to claim 1, wherein in the first nitride film forming step, the first nitride film is formed by an atomic layer deposition (ALD) method. 如申請專利範圍第1項之成膜方法,其中該第1氮化膜形成步驟係藉由從天線供給至該處理容器內之微波產生該第1反應氣體的電漿,從該天線供給至該處理容器內之微波的功率總和係2kW以上。 The film forming method of claim 1, wherein the first nitride film forming step generates a plasma of the first reaction gas by microwaves supplied from the antenna into the processing container, and supplies the plasma to the first reaction gas. The sum of the power of the microwaves in the processing vessel is 2 kW or more. 如申請專利範圍第1項之成膜方法,更包含第2氮化膜形成步驟,而該第2氮化膜形成步驟係在該第1氮化膜形成步驟後,藉由包含與該第1反應氣體不同之氣體的第2反應氣體的電漿,在該第1氮化膜上形成第2氮化膜。 The film forming method of claim 1, further comprising a second nitride film forming step, wherein the second nitride film forming step is performed after the first nitride film forming step A plasma of the second reaction gas of a gas having a different reaction gas forms a second nitride film on the first nitride film. 如申請專利範圍第4項之成膜方法,其中該第2反應氣體包含含有氫原子之氮化物的氣體。 The film forming method of claim 4, wherein the second reaction gas contains a gas containing a nitride of a hydrogen atom. 如申請專利範圍第4項之成膜方法,其中,藉由載置該被處理基板且設成可以一軸線為中心旋轉而使該被處理基板繞該軸線之周圍移動的載置台之旋轉,沿著該被處理基板相對於該軸線移動之周向,將該處理容器分成多數區域;該第1氮化膜形成步驟包含以下步驟:將前驅物氣體供給至該等多數區域中之一區域,使該前驅物氣體之分子吸附在該被處理基板之表面;將該第1反應氣體供給至該等多數區域中之另一區域;及藉由供給至該另一區域之微波產生該第1反應氣體的電漿,並藉由產生之電漿,對吸附有該前驅物氣體分子之該被處理基板的表面進行電漿處理,該第2氮化膜形成步驟包含以下步驟:在該一區域中將該前驅物氣體供給至處理容器內,使該前驅物氣體之分子吸附在該被處理基板之表面;將該第2反應氣體供給至該另一區域;及藉由供給至該另一區域的微波產生該第2反應氣體的電漿,並藉由產生之電漿,對吸附有該前驅物氣體分子之該被處理基板的表面進行電漿處理。 The film forming method of claim 4, wherein the substrate to be processed is placed and rotated about a single axis to rotate the substrate on which the substrate to be processed moves around the axis The processing container is divided into a plurality of regions in a circumferential direction in which the substrate to be processed is moved with respect to the axis; the first nitride film forming step includes the step of supplying a precursor gas to one of the plurality of regions, such that The molecules of the precursor gas are adsorbed on the surface of the substrate to be processed; the first reaction gas is supplied to another region of the plurality of regions; and the first reactant gas is generated by microwaves supplied to the other region a plasma, and a plasma treatment of the surface of the substrate to which the precursor gas molecules are adsorbed by the generated plasma, the second nitride film forming step comprising the steps of: The precursor gas is supplied into the processing container to adsorb molecules of the precursor gas on the surface of the substrate to be processed; the second reaction gas is supplied to the other region; and by supplying to the other The microwave plasma generating region of the second reaction gas, and by generating plasma, the surface adsorbed molecules of the precursor gas to be treated in the plasma processing of the substrate. 如申請專利範圍第4項之成膜方法,其中該第1氮化膜係以0.5nm至1.0nm之厚度形成於該含碳膜上。 The film forming method of claim 4, wherein the first nitride film is formed on the carbon-containing film with a thickness of 0.5 nm to 1.0 nm.
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